Archives June 2022

100 Days of Safe Production Compaign in 2022 Summer

The Group of Companies held the launching ceremony of the “100 Days of Safe Production Compaign in 2022 Summer”

On the morning of June 30, Junyuan Petroleum Group of Companies grandly held the launching ceremony of the 2022 summer production safety 100 day campaign with the theme of “reinforcing weaknesses, strengthening weaknesses, improving quality and ensuring safety” at the south side of the West conference room on the first floor of the new office building. More than 90 company leaders and employees, including Yu Rui, the Deputy General Manager of the Group, Wei Yu, the Deputy General Manager and Factory Director, and Qiao Huijie, the Deputy General Manager and Director of Safety and Environmental Protection, attended the event. The event was presided over by General Manager Qi Chunxiao. According to the agenda of the event, Chen Huimin, the Personnel Manager of the General Office, and Wei Fuchang, the Director of the Production and Operation Center, made a statement at the meeting. Qiao Huijie made a mobilization speech for the launch ceremony. After the event, the company’s leaders and employees signed the banner of the launch ceremony in turn. In his mobilization speech, Qiao Huijie pointed out that the company held the launching ceremony of the 2022 “100 days of Safe Production In summer”, which opened the prelude for all members of Junyuan Petroleum Group to participate in the 100 days of safe production in summer. This will play a positive and important role in improving safety awareness, improving the quality of employees, improving the construction of the company’s safety culture, and continuously promoting the stability and long-term development of the company’s safety situation.

Qiao Huijie said that this compaign has a long time span, including hot summer, Mid Autumn Festival and National Day important legal holidays. Today, with the increasingly urgent safety situation and the increasingly strict requirements of the state for work environment, we should take work safety more seriously. Although there are criticisms, controversies and unhappiness in our daily work, we will always be a family in dealing with safety issues, because our goal is to “Come to work happily and go home safely”. We all hope to live safely every day, and we hope that the whole staff will work together to pack up and achieve good results.

What products are involved in this 100 day safety production? What are the characteristics of these products?

Pentane is a fine chemical product. There are three isomers, namely n-Pentane, Isopentane and Cyclopentane, which are mainly used in polyurethane foam, EPS foaming agent, new hydrocarbon refrigerant for air conditioners and refrigerators, etc. The upstream of pentane industrial chain is the by-product of natural gas condensate, oil field light hydrocarbon, light naphtha ethylene unit cracking and the main product of C5, cyclopentadiene. The downstream is the application market, which is mainly concentrated in polyurethane foaming agent, EPS foaming agent, linear low-density polyethylene solvent and other fields.

Due to their different structures and properties, n-Pentane, Isopentane, Cyclopentane and Pentane Blend, have different application fields at present. n-Pentane can be isomerized to produce Isopentane, and can also be used as a foaming agent. It can also be used in low temperature thermometers, artificial ice, anesthetics, and the synthesis of pentanol; Isopentane is an important admixture to improve the octane number of gasoline, and it is also an important raw material for the production of isoprene. It can also be dehydrogenated, chlorinated and hydrolyzed to isoprene, isoprene and isopentanol. It is the raw material and solvent for organic synthesis; Cyclopentane is mainly used in organic synthesis and the production of intermediates of fine chemicals. At present, the market demand is low.

Luan Gaifeng / Department of Safety and Environmental Protection

 

70 Basic Concepts of Polyurethane

Understand 70 basic concepts of polyurethane, so that you can easily become a master of polyurethane

Polyurethane foam is derived from a mixture comprising a crude isocyanate component and a polyol component which contains all or some of the following products in a homogeneous mixture: polyols, catalysts, surfactants, water, flame-retardants, expanding agents, fillers, colourings, and pigments, in which the expanding agents comprise a pentane component associated with a diethanolamide derived from substances of vegetable origin. Polyurethane (PU) is a polymer that is made of different organic molecules (polyols and polyisocynates) that are bonded by urethane linkages. It can be either thermoplastic polyurethane (TPU) or thermosetting polyurethane. Pentanes are mainly known as blowing agents for insulation materials. But they can do even more: the three isomers n-Pentane, Isopentane and Cyclopentane can each show their advantages in a wide variety of applications, either on their own or as a blend. In this article you can read about the differences between the three Pentane isomers and the applications in which they have proven to be particularly useful.

1. Hydroxyl value: the amount of hydroxyl (-oh) contained in 1g polymer polyol is equivalent to the milligram of KOH, in mgkoh/g.
2. Equivalent: the average molecular weight of a functional group.
3. Isocyanate content: isocyanate content in the molecule
4. Isocyanate index: indicates the degree of excess isocyanate in polyurethane formula, usually represented by the letter R.
5. Chain extender: refers to low molecular weight alcohols and amines that can extend, expand or form spatial network crosslinks.
6. Hard segment: the segment on the main chain of polyurethane molecule formed by the reaction of isocyanate, chain extender and crosslinker. These groups have large cohesive energy, large space volume and large rigidity.
7. Soft segment: carbon carbon main chain polymer polyol with good flexibility. It is a flexible segment in the polyurethane main chain.
8. One step method: it refers to the method that oligomer polyol, diisocyanate, chain extender and catalyst are mixed at the same time, and then directly injected into the mold, and cured at a certain temperature.
9. Prepolymer method: the oligomeric polyol and diisocyanate are prepolymerized to form NCO terminated polyurethane prepolymer, and then the prepolymer is reacted with chain extender during pouring to prepare polyurethane elastomer, which is called prepolymer method.
10. Semi prepolymer method: the difference between semi prepolymer method and prepolymer method is that some polyester polyols or polyether polyols, chain extenders and catalysts are added to the prepolymer in the form of mixtures.
11. Reaction injection molding: also known as reaction injection molding (RIM), it is a process in which oligomers with small molecular weight are measured in liquid form, mixed instantaneously and injected into the mold at the same time, which react rapidly in the mold cavity, the molecular weight of the material increases rapidly, and a brand-new polymer containing new characteristic group structure is generated at an extremely fast speed.
12. Foaming index: that is, the number of parts of water equivalent to 100 parts of polyether is defined as foaming index (if).
13. Foaming reaction: generally refers to the reaction in which water reacts with isocyanate to generate substituted urea and release CO2.
14. Gel reaction: generally refers to the formation reaction of carbamate.
15. Gel time: the time required for liquid substances to form gel under certain conditions.
16. Opacification time: at the end of zone I, opacification occurs in the liquid-phase polyurethane mixed materials. This time is called cream time in the formation of polyurethane foam.
17. Chain extension coefficient: refers to the ratio of the amount of amino group and hydroxyl group (unit: mo1) in the chain extender component (including mixed chain extender) to the amount of NCO in the prepolymer, that is, the ratio of the molar number (equivalent number) of active hydrogen group to NCO.
18. Low unsaturation polyether: it is mainly developed for PTMG. The price of PPG is reduced to 0.05mol/kg, which is close to the performance of PTMG. DMC catalyst is used, mainly Bayer acclaim series products.
19. Urethane grade solvent: the solvent selected for the production of polyurethane should consider the solubility and volatilization rate, but the solvent used for the production of polyurethane should focus on the heavy nc0 group in polyurethane. Solvents such as alcohols, ethers and alcohols that react with NCO groups cannot be selected. The solvent shall not contain water, alcohol and other impurities, nor alkali substances, which will deteriorate the polyurethane.
Ester solvents are not allowed to contain water, free acids and alcohols, which will react with NCO groups. The ester solvent used for polyurethane shall be “urethane grade solvent” with high purity. That is, the solvent reacts with excess isocyanate, and then the amount of unreacted isocyanate is determined with dibutylamine to test whether it is suitable. The principle is that the one that consumes more isocyanates is not applicable, because it indicates that the water, alcohol and acid in the ester will consume the total value of isocyanates. If it is expressed in grams of solvent required to consume leqnco group, the higher the value, the better the stability.
Isocyanate equivalent less than 2500 shall not be used as polyurethane solvent.
The polarity of the solvent has a great influence on the reaction of the resin. The greater the polarity, the slower the reaction. For example, the difference between toluene and methyl ethyl ketone is 24 times. The polarity of this solvent molecule is large, and it can form hydrogen bond with the hydroxyl group of alcohol to slow the reaction.
Aromatic solvents are better for polychlorinated esters, and their reaction speed is faster than that of esters and ketones, such as xylene. The use of ester and ketone solvents can prolong the service life of the polyurethane In the production of coatings, the “urethane grade solvent” mentioned earlier in the film selection is beneficial to the stable parts stored.
Ester solvents have strong solubility, moderate volatilization rate, low toxicity and are used more. Cyclohexanone is also used more. Hydrocarbon solvents have low solid solubility and are rarely used alone. They are often used in combination with other solvents.
20. Physical foaming agent: physical foaming agent means that foam pores are formed through the change of physical form of a substance, that is, through the expansion of compressed gas, the volatilization of liquid or the dissolution of solid.
21. Chemical blowing agent: chemical blowing agent is a compound that can release carbon dioxide, nitrogen and other gases after heating and decomposition, and form fine pores in the polymer composition.
22. Physical crosslinking: there are some hard chains in the polymer soft chain, and the hard chain has the same physical properties as the vulcanized rubber after chemical crosslinking at the temperature below the softening point or melting point.
23. Chemical crosslinking: refers to the process in which macromolecular chains are connected by chemical bonds under the action of light, heat, high-energy radiation, mechanical force, ultrasound and crosslinking agent to form a network or body structure polymer.
24. Foaming index: the number of parts of water equivalent to 100 parts of polyether is defined as foaming index (if).
25. what are the commonly used isocyanates in terms of structure?
Answer: aliphatic: HDI, alicyclic: IPDI, htdi, hmdi, aromatic: TDI, MDI, Papi, PPDI, NDI.
26. what kinds of isocyanates are commonly used? Write the structure
Answer: toluene diisocyanate (TDI), diphenylmethane-4,4 ‘- diisocyanate (MDI), polyphenylmethane polyisocyanate (Papi), liquefied MDI, hexamethylene diisocyanate (HDI).
27. What are the meanings of tdi-100 and tdi-80?
Answer: tdi-100 refers to toluene diisocyanate with 2,4 structure; Tdi-80 refers to a mixture composed of 80% toluene diisocyanate with 2,4 structure and 20% 2,6 structure.
28. What are the characteristics of TDI and MDI in the synthesis of polyurethane materials?
A: for the reactivity of 2,4-TDI and 2,6-TDI. The reaction activity of 2,4-TDI is several times higher than that of 2,6-TDI, because the NCO at position 4 in 2,4-TDI is far away from the NCO at position 2 and methyl group, and there is almost no steric hindrance, while the NCO of 2,6-TDI is greatly affected by the steric hindrance effect of ortho methyl group, so the reaction activity is affected.
The two NCO groups of MDI are far away from each other, and there are no substituents around, so the activities of these two NCOs are large. Even if one NCO participates in the reaction, the activities of the remaining NCOs are reduced, and the overall activity is still large. Therefore, the reaction activity of MDI polyurethane prepolymer is greater than that of TDI prepolymer.
29. Which of HDI, IPDI, MDI, TDI and NDI has better yellowing resistance?
Answer: HDI (belonging to invariant yellow aliphatic diisocyanate) and IPDI (the polyurethane resin made has excellent optical stability and chemical resistance, and is generally used to manufacture high-grade non discolored polyurethane resin).
30. Purpose of MDI modification and common modification methods
A: Liquefied MDI: modification purpose: Liquefied pure MDI is a kind of MDI modified by liquefaction. It overcomes some defects of pure MDI (solid at room temperature, melting when used, and the performance is affected by repeated heating). It also provides a basis for large-scale modification to improve the performance of MDI based polyurethane materials.
method:
① Urethane modified liquefied MDI.
② Carbodiimide and uretonimine modified liquefied MDI.
31. what types of polymer polyols are commonly used?
Answer: polyester polyol, polyether polyol
32. how many industrial production methods are there for polyester polyols?
Answer: A. vacuum melting method B. carrier gas melting method C. azeotropic distillation method
33. what are the special structures on the molecular backbone of polyester and polyether polyols?
Answer: polyester polyol: a macromolecular alcohol compound containing ester group on the main chain and hydroxyl (-oh) on the end group. Polyether polyol: polymer or oligomer containing ether bond (-o-) and terminal group (-oh) or amino group (-nh2) in the molecular main chain structure.
34. according to the characteristics, polyether polyols are divided into several categories?
Answer: high activity polyether polyol, grafted polyether polyol, flame retardant polyether polyol, heterocyclic modified polyether polyol, polytetrahydrofuran polyol.
35. how many kinds of ordinary polyether are there according to the initiator?
Answer: polyoxypropylene glycol, polyoxypropylene triol, hard foam polyether polyol, low unsaturation polyether polyol.
36. what is the difference between hydroxyl terminated polyether and amino terminated polyether?
Amine terminated polyether is a polyoxypropylene ether whose hydroxyl end is substituted by amino group.
37. what types of polyurethane catalysts are commonly used? Which common varieties are included?
Answer: the common types of tertiary amine catalysts are: triethylenediamine, dimethyl ethanolamine, N-methyl morphorphine, N, N-dimethyl cyclohexylamine
Metal alkyl compounds, common varieties are: organotin catalysts, which can be divided into stannous octanoate, stannous oleate, dibutyltin dilaurate.
38. what are the commonly used polyurethane chain extenders or crosslinkers?
Answer: Polyols (1,4-butanediol), alicyclic alcohols, aromatic alcohols, diamines, alcohol amines (ethanolamine, diethanolamine)
39. reaction mechanism of isocyanate
Answer: the reaction between isocyanate and active hydrogen compound is caused by the nucleophilic center in the active hydrogen compound molecule attacking the carbon atom of NCO group. The reaction mechanism is as follows:
40. how does the isocyanate structure affect the reactivity of NCO groups?
Answer: electronegativity of A.R group: if R group is electron absorbing group, the electron cloud density of C atom in -nco group will be lower and more vulnerable to attack by nucleophiles, that is, it is easier to conduct nucleophilic reaction with alcohols, amines and other compounds. If R is an electron donor group, the electron cloud density of C atom in -nco group will increase through electron cloud transmission, making it less vulnerable to attack by nucleophiles, and its reaction ability with compounds containing active hydrogen will decrease. B. Induction effect: because the aromatic diisocyanate contains two NCO groups, when the first NCO gene participates in the reaction, due to the conjugation effect of the aromatic ring, the -nco group that does not participate in the reaction will play the role of electron withdrawing group and enhance the reaction activity of the first NCO group, which is the induction effect. C. Steric hindrance effect: in the aromatic diisocyanate molecule, if two -nco groups are on an aromatic ring at the same time, the influence of one NCO group on the reaction activity of the other NCO group is often significant. However, when two NCO groups are located on different aromatic rings in the same molecule, or they are separated by hydrocarbon chains or aromatic rings, the interaction between them is small, and decreases with the increase of the length of chain hydrocarbons or the number of aromatic rings.
41. types of active hydrogen compounds and NCO reactivity
Answer: aliphatic nh2> aromatic nh2> primary oh> water > secondary oh> phenolic oh> carboxyl group > substituted urea > amide > carbamate. (if the electron cloud density of nucleophilic center is higher, its electronegativity is stronger, and its reaction activity with isocyanate is higher, and the reaction speed is faster; otherwise, its activity is lower.)
42. effect of hydroxyl compounds on their reactivity with isocyanates
Answer: the reactivity of active hydrogen compounds (Roh or rnh2) is related to the properties of R. when R is an electron withdrawing group (with low electronegativity), it is difficult to transfer hydrogen atoms, and the reaction between active hydrogen compounds and NCO is more difficult; If R is an electron donor substituent, the reactivity of active hydrogen compounds with NCO can be improved.
43. what is the purpose of the reaction of isocyanate with water
Answer: it is one of the basic reactions for preparing polyurethane foam. The reaction between them first generates unstable carbamic acid, and then decomposes into CO2 and amine. If the isocyanate is excessive, the generated amine will react with the isocyanate to generate urea.
44. during the preparation of polyurethane elastomers, the water content of polymer polyols shall be strictly controlled
Answer: no bubbles are required in elastomers, coatings and fibers, so the water content in raw materials must be strictly controlled, usually less than 0.05%.
45. difference of catalytic effect of amine and tin catalysts on isocyanate reaction
Answer: tertiary amine catalysts have high catalytic efficiency for the reaction of isocyanate with water, while tin catalysts have high catalytic efficiency for the reaction of isocyanate with hydroxyl.
46. why can polyurethane resin be regarded as a block polymer? What are the characteristics of the chain segment structure?
Answer: the chain segment of polyurethane resin is composed of hard segment and soft segment. The hard segment refers to the chain segment formed by the reaction of isocyanate, chain extender and crosslinker on the main chain of polyurethane molecule. These groups have large cohesive energy, large space volume and large rigidity. The soft segment refers to the carbon carbon main chain polymer polyol, which has good flexibility and is a flexible segment in the polyurethane main chain.
47. what are the factors that affect the properties of polyurethane materials?
Answer: cohesive energy of group, hydrogen bond, crystallinity, crosslinking degree, molecular weight, hard segment and soft segment
48. what are the raw materials for the soft and hard segments of the main chain of polyurethane materials
Answer: the soft segment is composed of oligomer Polyols (polyester, polyether glycol, etc.), and the hard segment is composed of polyisocyanate or its small molecule chain extender.
49. how do the soft and hard segments affect the performance of polyurethane materials?
Answer: soft segment: (1) molecular weight of soft segment: assuming that the molecular weight of polyurethane is the same, if the soft segment is polyester, the strength of polyurethane will increase with the increase of molecular weight of polyester glycol; If the soft segment is polyether, the strength of polyurethane decreases with the increase of molecular weight of polyether glycol, but the elongation increases. (2) Crystallinity of soft segment: it contributes greatly to the crystallinity of linear polyurethane segment. Generally speaking, crystallinity is beneficial to improve the performance of polyurethane products, but sometimes crystallization will reduce the low-temperature flexibility of materials, and crystalline polymers are often opaque.
Hard segment: the hard segment usually affects the softening melting temperature and high temperature performance of the polymer. The polyurethane prepared by aromatic isocyanate has a rigid aromatic ring in its hard segment, so its hard segment cohesion strength increases. The material strength is generally greater than that of aliphatic isocyanate polyurethane, but its UV degradation resistance is poor and it is easy to yellowing. Aliphatic polyurethane will not turn yellow.
50. classification of polyurethane foam
Answer: (1) hard foam and soft foam; (2) high density and low density foam; (3) polyester and polyether foam; (4) TDI and MDI foam; (5) polyurethane foam and polyisocyanurate foam; (6) one-step and prepolymerization production; (7) continuous and intermittent production; and (8) block foam and molded foam.
51. basic reaction of foam preparation
Answer: it refers to the reaction between -nco and -oh, -nh2 and H2O. When it reacts with polyols, the “gel reaction” in the foaming process generally refers to the formation reaction of carbamate. Because the foam raw material uses multi-functional raw materials, the crosslinked network is obtained, which makes the foaming system quickly gel.
Foaming reaction occurs in the foaming system with water. The so-called “foaming reaction” generally refers to the reaction in which water reacts with isocyanate to generate substituted urea and release CO2.

52. nucleation mechanism of bubbles
The raw material reacts in the liquid or depends on the temperature of reaction production to produce gaseous substances and volatilize the gases. With the progress of the reaction and the large amount of reaction heat, the amount of gaseous substances and volatilization is increasing. When the gas concentration increases beyond the saturation concentration, the maintained bubbles begin to form in the solution phase and rise.
53. the role of foam stabilizer in the preparation of polyurethane foam
Answer: it has emulsification function, which enhances the mutual solubility of each component of foam material; After adding silicone surfactant, the surface tension of the liquid is greatly reduced γ , The increased free energy required for gas dispersion is reduced, which makes the air dispersed in the raw material easier to nucleate in the mixing process, helps to produce small bubbles and improves the stability of foam.
54. stability mechanism of foam
Answer: the addition of appropriate surfactant is conducive to the formation of fine bubble dispersion.
55. formation mechanism of open cell foam and closed cell foam
Answer: formation mechanism of open cell foam: in most cases, when the maximum pressure is generated in the bubble, the strength of the bubble wall formed by the gel reaction is not high, and it cannot withstand the wall membrane tension caused by the increase of gas pressure. The bubble wall membrane is pulled and broken, and the gas escapes from the rupture to form open cell foam.
Formation mechanism of closed cell foam: for hard foam system, due to the reaction of polyether polyols with multi-functional and low molecular weight with polyisocyanate, the gel speed is relatively fast, and the gas in the cell can not break the cell wall, thus forming a closed cell foam.
56. foaming mechanism of physical foaming agent and chemical foaming agent
Answer: physical foaming agent: physical foaming agent means that foam pores are formed through the change of physical form of a substance, that is, through the expansion of compressed gas, the volatilization of liquid or the dissolution of solid.
Chemical blowing agent: chemical blowing agent is a compound that can release carbon dioxide, nitrogen and other gases after heating and decomposition, and form fine pores in the polymer composition.
57. preparation method of flexible polyurethane foam
Answer: one step and prepolymer method
Prepolymer method: the prepolymer containing free NCO group is prepared by the reaction of polyether polyol and excess TDI, and then mixed with water, catalyst, stabilizer, etc. to make foam.. One step method: various raw materials are directly mixed in the mixing head through calculation to produce foamed plastics in one step, which can be divided into continuous type and intermittent type.
58. characteristics of horizontal foaming and vertical foaming
Answer: characteristics of horizontal foaming: side film lifting method: this method adds an upward traction side paper device on the basis of the original horizontal foaming machine to make the edge and middle of foam rise and foam synchronously, so as to make a foam block close to the flat top. Balanced pressing plate method: it is characterized by the use of top paper and top cover plate. Overflow trough method: characterized by the use of overflow trough and conveyor belt landing plate.
Vertical foaming features: large cross-sectional area of foam blocks can be obtained with a small flow rate, while the horizontal foaming machine is usually used to obtain blocks with the same cross-section, and the horizontal flow rate is 3 ~ 5 times larger than the vertical foaming; Because the cross section of the foam block is large, there is no upper and lower skin, and the side skin is thin, so the cutting loss is greatly reduced; The equipment covers a small area, the plant height is about 12 ~ 13m, and the investment cost of plant and equipment is lower than that of horizontal foaming process; The cylindrical or rectangular foam body can be produced conveniently by changing the hopper and model, especially the round block foam blank for rotary cutting.
59. basic points of raw material selection for soft foam preparation
Answer: polyols: polyether polyols used for ordinary block foam, with a molecular weight of 3000 ~ 4000, mainly polyether triols. High resilience foam mostly uses polyether triol with molecular weight of 4500 ~ 6000. When the molecular weight increased, the tensile strength, elongation and resilience of foam increased; The reactivity of the same polyether decreased. When the functionality of polyether is increased, the reaction is relatively accelerated, the crosslinking degree of polyurethane is increased, the hardness of foam is increased, and the elongation is decreased. Isocyanate: toluene diisocyanate (tdi-80) is the main Isocyanate Raw Material of polyurethane soft block foam. Tdi-65 with relatively low activity is only used for polyester polyurethane foam or special polyether foam. Catalysts: the catalysts used for block soft foam foaming can be roughly divided into two categories: one is organometallic compounds, of which stannous octanoate is the most commonly used; The other is tertiary amine, commonly used as bis (dimethylaminoethyl) ether. Foam stabilizer: the polyester type polyurethane block foam is mainly composed of non silicon surfactants, and the polyether type block foam is mainly composed of silicone olefin oxide copolymers. Foaming agent: generally, when manufacturing polyurethane soft block foam with a density greater than 21 kg / m3, only water is used as foaming agent; Only low boiling point compounds such as methylene chloride (MC) are used as auxiliary blowing agents in low-density formulations.
60. influence of environmental conditions on physical properties of block foam
Answer: influence of temperature: the foaming reaction of polyurethane accelerates with the rise of material temperature, which will cause the risk of core burning and fire in sensitive formulas. Influence of air humidity: with the increase of humidity, the hardness of foam decreases and the elongation increases because the isocyanate group in foam reacts with the moisture in the air; The tensile strength of foam increased due to the increase of urea group. Effect of atmospheric pressure: for the same formula, when foaming at a higher altitude, the density decreases significantly.
61. main differences of raw material system between cold molded soft foam and hot molded foam
Answer: the raw materials used for cold curing molding have high reactivity. During curing, there is no need for external heating. Depending on the heat generated by the system, the curing reaction can be basically completed in a short time, and the raw materials can be demoulded within a few minutes after injection molding. The raw material reaction activity of heat curing molding foam is low. After the reaction mixture is foamed in the mold, it needs to be heated together with the mold. The foam products can be demoulded only after they are completely cured in the drying channel.
62. what are the characteristics of cold molded soft foam compared with hot molded foam
Answer: ① there is no need to provide external heat in the production process, which can save a lot of heat energy; ② High sag coefficient and good comfort; ③ High rebound rate; ④ Foam without flame retardant also has certain flame retardancy; ⑤ The production cycle is short, which can save the mold and cost.
63. characteristics and applications of soft foam and hard foam
Answer: characteristics of soft foam: the cell structure of polyurethane soft foam is mostly open cell. Generally, it has the properties of low density, good elastic recovery, sound absorption, ventilation, heat preservation, etc. Application: mainly used as furniture, cushion material, vehicle seat cushion material, various soft cushion laminated composite materials. In industry and civil use, soft foam is also used as filter material, sound insulation material, shockproof material, decorative material, packaging material, heat insulation material, etc.
Characteristics of rigid foam: polyurethane foam has light weight, high specific strength and good dimensional stability; Polyurethane rigid foam has superior thermal insulation performance; Strong adhesion; Good aging performance and long thermal insulation service life; The reaction mixture has good fluidity and can smoothly fill the mold cavity or space with complex shapes; The raw materials for the production of polyurethane rigid foam are highly reactive, which can realize rapid curing, and can realize high-efficiency and mass production in the factory.
Uses: used as insulation materials for refrigerators, freezers, refrigerated containers, cold storages, etc., insulation layers for oil transmission pipelines and hot water transmission pipelines, insulation layers for building walls and roofs, insulation sandwich panels, etc.
64. key points of hard foam formula design
Answer: polyols: polyether polyols used in hard foam formulation are generally polyoxypropylene polyols with high functionality and high hydroxyl value (low molecular weight); Isocyanate: at present, the isocyanate used for hard foam is mainly polymethylene polyphenyl polyisocyanate (commonly known as Papi), i.e. crude MDI and polymerized MDI; Blowing agent: (1) CFC blowing agent (2) HCFC and HFC blowing agent (3) pentane blowing agent (4) water; Foam stabilizer: the foam stabilizer used for polyurethane rigid foam formulation is generally a block polymer of polydimethylsiloxane and polyolefin. At present, most foam stabilizers are mainly Si-C type; Catalyst: the catalyst of hard foam formula is mainly tertiary amine, and organotin catalyst can be used in special occasions; Other additives: according to the requirements and needs of different uses of polyurethane rigid foam products, flame retardant, pore opening agent, smoke inhibitor, antioxidant, mildew inhibitor, toughening agent and other additives can also be added to the formula.
65. preparation principle of whole skin molded foam
Answer: integral skin foam (ISF), also known as self skinning foam, is a kind of foam that produces a dense skin during manufacturing.
66. characteristics and applications of polyurethane microporous elastomer
A: characteristics: polyurethane elastomer is a block polymer, which generally consists of oligomer polyol flexible long chain to form soft segment, diisocyanate and chain extender to form hard segment, and hard segment and soft segment are arranged alternately to form repeated structural units. In addition to containing urethane groups, polyurethane can form hydrogen bonds within and between molecules, and the soft and hard segments can form microphase regions and generate microphase separation.
67. what are the main performance characteristics of polyurethane elastomer
Answer: performance characteristics: 1. High strength and elasticity, which can maintain high elasticity in a wide hardness range (Shore A10 ~ shore d75); Generally, the required low hardness can be achieved without plasticizer, so there is no problem caused by plasticizer migration; 2. Under the same hardness, the bearing capacity is higher than that of other elastomers; 3. Excellent wear resistance, its wear resistance is 2 ~ 10 times that of natural rubber; 4. Excellent oil and chemical resistance; Aromatic polyurethane radiation resistance; Excellent oxygen resistance and ozone resistance; 5. High impact resistance, fatigue resistance and vibration resistance, suitable for high-frequency flexure applications; 6. Good low temperature flexibility; 7. Ordinary polyurethane can not be used above 100 ℃, but it can withstand 140 ℃ high temperature with special formula; 8. Molding and processing costs are relatively low.
68. polyurethane elastomers are classified according to polyols, isocyanates, manufacturing processes, etc
Answer: 1 According to the raw materials of oligomer polyols, polyurethane elastomers can be divided into polyester type, polyether type, polyolefin type, polycarbonate type, etc. the polyether type can be divided into polytetrahydrofuran type, polyoxypropylene type, etc. according to specific varieties; 2. according to different diisocyanates, they can be divided into aliphatic and aromatic elastomers, which can be subdivided into TDI, MDI, IPDI, NDI and other types; In terms of manufacturing process, polyurethane elastomers are traditionally divided into three categories: casting type (CPU), thermoplastic type (TPU) and mixing type (MPU).
69. from the perspective of molecular structure, what are the factors that affect the properties of polyurethane elastomers?
Answer: from the perspective of molecular structure, polyurethane elastomer is a block polymer. Generally, the soft segment is composed of oligomer polyol flexible long chain, and the hard segment is composed of diisocyanate and chain extender. The hard segment and soft segment are arranged alternately to form repeated structural units. In addition to containing urethane groups, polyurethane can form hydrogen bonds within and between molecules, and the soft and hard segments can form microphase regions and generate microphase separation. These structural characteristics make polyurethane elastomer have excellent wear resistance and toughness, and it is known as “wear-resistant rubber”.
70. performance difference between ordinary polyester type and polytetrahydrofuran ether type elastomers
Answer: Polyester molecules contain more polar ester groups (-coo-), which can form strong intramolecular hydrogen bonds. Therefore, polyester polyurethane has high strength, wear resistance and oil resistance.
The elastomer prepared from polyether polyol has good hydrolytic stability, weather resistance, low temperature flexibility and mold resistance.

Where do Pentanes come from?
Pentanes are all saturated hydrocarbons that have five carbon atoms. n-Pentane and iso-Pentane occur naturally in crude oil and as a by-product of natural gas production. Cyclopentane, a ring-shaped molecule much sought after by the industry, is found more in naphtha (crude petrol), which is obtained in refineries from so-called cracking processes.

Naphtha contains varying amounts of Pentanes, depending on the origin of the crude oil, the construction of the refinery and the management of the processes. They are the first hydrocarbons to be liquid at room temperature.

Isopentane has the lowest boiling point at 29 °C, followed by n (35 °C) and Cyclopentane (49 °C). Due to the low boiling points and the large interval between them, the three isomers of Pentane can be easily separated from each other.

Pentane production: What are the differences between n-Pentane, Isopentane and Cyclopentane?
Due to their property profile, Isopentane, n and Cyclopentane can show their advantages in a wide variety of applications. Moreover, the three isomers can be mixed with each other or with other chemical components. In this way, it is possible to create Pentane blends that fulfil the desired requirement profile in the best possible way.

Application area Isopentane
Isopentane is almost insoluble in water, but shows very good solubility or unlimited miscibility with many organic solvents such as paraffins, ethers, esters, aromatics or chlorinated hydrocarbons. Therefore, the product is suitable for a wide range of applications:

Personal care products such as shaving foam and shower gel
Working medium in geothermal plants
Non-polar solvent with very high volatility
Process medium for polyethylene (PE, LLDPE) and polypropylene (PP)

The company went to Dongming Petrochemical Group to carry out technical exchanges

The company went to Dongming Petrochemical Group to carry out technical exchangesAt the invitation of Shandong Dongming Petrochemical Group Co., Ltd., Liu Yangbing, the Manager of the company’s Sales Department, and a delegation of four people went to Dongming Petrochemical Group to carry out technical exchanges on n-hexane products on June 29. The leaders of Dongming Petrochemical extended a warm welcome to the arrival of our exchange group. The two sides had a deep and detailed conversation on our company’s product quality, production technology, production capacity, product consumption and technical requirements of Dongming Petrochemical, and had full communication and negotiation on cooperation matters. Through this exchange and investigation, the mutual understanding between the two sides was deepened, and the cooperation ideas were further clarified, laying a solid foundation for the later in-depth cooperation. Tingting Chang/ Sales Department

market supply and demand changes from raw material prices

Pentane blowing agent: market supply and demand changes from raw material prices

Since 2022, affected by the strong rise in the crude oil market, the price of Domestic Topping oil has risen as a whole, and the profits of downstream pentane foaming agent manufacturers once entered a negative range. In the middle of March, the crude oil began to fall after rising, the price of Domestic Topping oil began to decline, the profits of pentane blowing agent manufacturers improved, and the manufacturers began to operate one after another.

Taking Shandong as an example, it can be seen from the above figure that since 2022, the prices of topping oil and pentane foaming agent in the region have increased. However, from January to February, the price of raw materials has increased too fast, which has been higher than the price of foaming agent products for a long time. Considering the freight of raw materials, the processing cost of devices and other factors, the device has suffered obvious losses. The foaming agent factories in Dongying have shut down one after another, and the supply has declined. At present, the total capacity of pentane units in the Chinese market is about 3million tons, the daily theoretical supply is about 8200 tons / day, and the actual daily output is about 5800 tons. By the middle of March, it was more difficult to find goods downstream.

However, in the middle of June, the domestic refined oil market demand was poor. In particular, the epidemic situation in Shandong repeatedly led to the upgrading of management and control, many regions entered the state of home isolation, and the reduction of travel further weakened the gasoline consumption. As of June 29, the national VI 92. It is understood that the unit of Daqing Oilfield fine chemical industry was restarted on June 12, Dongying Liangxin Petrochemical Technology Development Limited Company resumed construction around March 15, and Shida Changsheng plans to resume construction on March 15, resulting in an increase in market supply.

As for the future market, the supply of pentane blowing agent in the Chinese market will remain stable from mid to late March to June. In terms of raw materials, there are certain guidelines on the news. The market has digested in advance the benefits of supply tightening brought about by the overhaul of Huaxing, Changyi, Zoje, etc. at present, it is mainly supported by downstream demand. By early April, there was a small and long Tomb Sweeping Day holiday in China. Although the epidemic situation has been repeated to a certain extent, there are still some goods in the domestic gasoline market, supporting the acceleration of raw material shipment and supporting the pentane foaming agent market. The downstream EPS market of foaming agent is expected to be better as the temperature warms up. Overall, the pentane blowing agent market maintained good supply and demand from mid March to June.

Cyclopentane, as a blowing agent in Polyurethane (PU) foams, is the most important raw material for high-performance insulation in refrigerators

High Purity Production Technology of Cyclopentane

Cyclopentane, also known as pentamethylene, is a kind of hydrocarbon. It is used to replace freon as a foaming agent for refrigerator freezer insulation materials and hard PU foam. It is used as a solvent for solution polymerization of polyisoprene rubber and cellulose ether. Isopentane is one of the components of petroleum ether. It is obtained through the recombination of isopentane under the action of platinum. It has a broad market prospect. High purity industrial grade requires high cyclopentane itself, so it is of great significance to strengthen the research on purification technology of high purity cyclopentane.
Cyclopentane has low thermal conductivity, good anti-aging performance, no damage to the ozone layer, and many advantages in solubility in polyols. At present, cyclopentane production mainly relies on petrochemical raw materials, mainly petrochemical C5 fraction. Cyclopentane is a component of petroleum ether in the boiling point range of 30-60 ℃, and its content is generally 5%-10%. It is distilled under normal pressure in a 8m high tower with a reflux ratio of 60:1. Isopentane and n-pentane are first evaporated, and then fractionated to obtain cyclopentane with a purity of more than 98%. Cyclopentane can also be prepared by reduction of Cyclopentanone or catalytic hydrogenation of cyclopentadiene.

Cyclopentane Blowing Agent

The spontaneous combustion temperature of cyclopentane blowing agent is about 380 ℃. The normal temperature of 50 ℃ will not cause spontaneous combustion. Harmful effects of cyclopentane inhalation of high concentrations of cyclopentane can cause central nervous system depression, although its acute toxicity is low. The symptoms caused by acute exposure are first excitement, then imbalance, even numbness and coma. Rarely die of respiratory failure. It has been reported that this product was given orally to animals, resulting in severe diarrhea, heart, lung and liver vascular collapse and brain degeneration.

Cyclopentane and Freon are both substances that are easy to liquefy and vaporize. They should absorb heat during vaporization and release heat during liquefaction; Liquid cyclopentane flows in the pipe. When it flows to the freezer, it will vaporize and absorb heat, absorbing the heat in the refrigerator and reducing the temperature in the refrigerator; When it flows into the condenser, it will be compressed and liquefied, and the absorbed heat will be released to achieve the purpose of refrigeration.
In the past, most of the traditional water tank insulation materials in the solar industry used polyurethane foaming technology. This material has many disadvantages, such as consuming oil resources, destroying the ozone layer with HCFC-141b foaming agent, and “white pollution” caused by waste foam. It does not meet the environmental protection requirements. Cyclopentane, as a new environmentally friendly foaming agent, has brought greater improvement to our environment and life, but cyclopentane is flammable and volatile, It is easy to cause combustion and explosion in case of open fire. Pay special attention to safety during use.

Junyuan Petroleum Group is a new chemical enterprise integrating R & D, production and marketing. The company’s products cover four major fields: refrigerant, carbon hydride, fluoride and chemical raw materials. Its main products are n-pentane and isopentane Pentane blowing agent, n-hexane, isohexane, n-heptane, n-octane, petroleum ether, isobutane R600a, n-butane R600, propane R290, propylene R1270, n-pentane r601, isopentane r601a, cyclopentane, isobutene, ethylene R1150, R22, R23, r507, ethane R170, methane, freon, dimethyl ether, isooctane, n-heptane, propylene butane, n-hexane, n-hexene, n-butene and other blowing agents, aerosols and solvents; The company is committed to science and technology and environmental protection industries. Its products are widely used in refrigeration, energy, electronics, pharmaceutical intermediates, scientific research, laser technology, aerospace technology, metal smelting, low-temperature refrigeration and other fields. Its customers radiate in Europe, America, the Middle East and Southeast Asia.

Pentane blowing agents for polyurethane foams

Pentane blowing agents for polyurethane foams

Pentanes as blowing agents in insulating foams, which are largely responsible for the excellent performance of the insulating materials. All three isomers of Pentane are used: n-Pentanes, Isopentanes and Cyclopentanes. It is particularly important for manufacturers of insulating materials to have high quality, individual blend compositions and tailor-made formulations. Insulating materials for refrigerators or the construction industry depend on Pentanes as an important blowing agent for insulating foams. This makes it all the more important to have high-quality n-Pentanes, Isopentanes and Cyclopentanes from a reliable supplier:

Blowing Agent Manufacturer

Junyuan Petroleum Group is an ISO Certified company. Junyuan Petroleum Group is engaged in manufacturing and exporting specialty solvents. Our solvents caters to a large variety of EPS products manufacturers. We established ourselves as one of the leading manufacturers and exporters of Industrial chemicals and its derivatives in China. On strength of our competent, energetic, experienced, skilled and dedicate R&D team, we have evolved and provided several pentanes and their blends. We cater to the industries engaged in EPS product manufacturing. We cater to a variety of industrial chemical to reputed companies world wide. As we are industrial chemical manufacturer in China with the confidence put in our capabilities & services, we intend to grow as an honest & preferred co-partner to customers having requirements of regular and new molecules which require sophisticated plastic and construction chemistry.
Junyuan Petroleum Group has made its name as most trusted blowing agent manufacturer in Dongying, China. Blowing agents of all types are produced and supplied by Junyuan Petroleum Group all across China. As the best industrial chemical manufacturer in China, Junyuan Petroleum Group has always given importance to its client satisfaction. Timely delivery of our blowing agents are guaranteed by our company.We are dealing in n-Pentane, Isopentane, Cyclopentane, Pentane Blends, Blowing Agents, Pentane 80/20, Pentane 60/40, Pentane 75/25, Pentane 50/50, Pentane 70/30, Pentane 85/15 and Pentane 90/10 etc.

Blowing agent choice per application

In contrast to HCFC141b, where one blowing agent was chosen for all rigid foam applications, different blowing agent choices will be available after the HCFC phase out. Pentane is generally preferred when the foam consumption is high (e.g. in board or panel lamination). In the following figure, the blowing agent choice in industrialised countries is schematically given.
The three corners of the triangle represent a situation where a market segment has been entirely converted to pentane, HFC or to a fully water blown solution. Positions within the triangle indicate the relative amount of producers within a segment, that have chosen any of the three blowing agent options.

Blowing Agent, Pentane Blend, Blowing Agents, Pentane Blends
Blowing Agent, Pentane Blend, Blowing Agents, Pentane Blends

The physical properties of blowing agents are given in the table.

It is interesting to note the differences between the three pentane isomers. There are significant differences in boiling point, gas thermal conductivity and polyol solubility, which leads to very different foam properties and processing characteristics. Cyclo/iso pentane mixtures tend to produce the lowest thermal conductivity foams and are preferred in applications such as refrigerators. Cyclopentane is, in certain cases, preferred when local storage regulations are less stringent than for other pentanes.

Physical properties of blowing agents
Physical properties of blowing agents
Properties of other blowing agents relative to HCFC141b
Properties of other blowing agents relative to HCFC141b

What is Polyurethane Foam?

The great advantages of polyurethane foams are their ability to respond to specific requirements for each application (e.g. density, elasticity and durability) and at prices which make the end products well in reach of the average household. It is estimated that 90% of upholstered furniture has a polyurethane foam filling.

Blowing agent evolution
Blowing agent evolution

The gas phase thermal conductivity of pentane blowing agents

The gas phase thermal conductivity of Cyclopentanes is the lowest among alkane blowing agents. It has relatively high solubility in polyether polyols and is the largest amount of alkane blowing agent. Polyurethane rigid foam Cyclopentane foaming system was industrialized in 1993, mainly used as refrigerator insulation materials. According to Bayer company of Germany, more than 3 million refrigerators have been produced in Europe with its Cyclopentane foaming formula in 1994. Because the boiling point of Cyclopentane is higher than room temperature, part of the cycloalkane gas in the foamed cell condenses and plasticizes the polyurethane matrix. Therefore, in order to achieve the minimum compressive strength required for the stability of foam, the density of foam is higher than that of CFC 11. The foaming foam is more than 10% (the foam density of the refrigerator insulation layer should be more than 38 kg/mJ). Its thermal conductivity is also high.

Comparison of n-pentane, isopentane and cyclopentane foaming systems

n-Pentane and Isopentane are rich in natural resources, and their prices are lower than Cyclopentane. Due to their higher gas-phase thermal conductivity and low solubility in polyether, n-Pentane and Isopentane are rarely used alone in the refrigerator industry. n-/Isopentane mixture is mainly used as blowing agent for rigid polyurethane foam for construction. Since 1994, the company has adopted Isopentane (75/25) foaming system to reduce the minimum stable density of foam to 32, but the thermal conductivity has increased by about 10%. However, due to the uniform density distribution of Pentane blowing foam, the adiabatic energy consumption is only 2% to 5% higher than that of CFC-11 system. The n-/Isopentane (75/25) foaming system developed by Junyuan Petroleum Group also obtained similar results. The stable density of the refrigerator body is about 34, while the thermal conductivity of the foam at 10 ℃ is 2lmw/ (MK), only lmw/ (MK) higher than that of the cyclopentane foam.

Polyolefin foams made with isopentane-based blowing agents

Polyolefin foams made with isopentane-based blowing agents
A blowing agent blend for making polyolefin foams comprising isopentane and at least one co-blowing agent The co-blowing agent is either a physical co-blowing agent having a boiling point less than 28° C., or a chemical co-blowing agent, or combinations thereof The blowing agent blend comprises less than about 99 mol % isopentane.

Inventors:
Handa, Paul Y. (Pittsford, NY, US)
Gu, Jiayan (Farmington, NY, US)
Application Number:
10/188263
Publication Date:
01/08/2004
Filing Date:
07/02/2002
Assignee:
HANDA Y. PAUL
GU JIAYAN
Other Classes:

516/12
International Classes:
C08J9/12; C08J9/14; (IPC1-7): C08J9/00


Primary Examiner:

FOELAK, MORTON
Attorney, Agent or Firm:
NIXON PEABODY LLP (CHICAGO, IL, US)
Claims:

What is claimed is:



1. A blowing agent blend for making polyolefin foams comprising isopentane and at least one co-blowing agent, the co-blowing agent being either a physical co-blowing agent having a boiling point less than 28° C., or a chemical co-blowing agent, or combinations thereof, and wherein the blowing agent blend comprises less than about 99 mol % isopentane.

2. The blowing agent blend of claim 1, wherein the polyolefin foam is dimensionally stable.

3. The blowing agent blend of claim 1, wherein the co-blowing agent includes at least one physical co-blowing agent, the at least one physical co-blowing agent being ethane, n-propane, n-butane, isobutane, cyclopropane, nitrogen, argon, carbon dioxide, sulfur hexafluoride, nitrous oxide, dimethyl ether, 1,1-difluoroethane (HFC-152a), 1,1,1-trifluoroethane (HFC-143a), 1,1,1,2-tetrafluoroethane (HFC-134a), 1,1,2,2-tetrafluoroethane (HFC-134), 1,1,1,3,3-pentafluoropropane (HFC-245fa) or combinations thereof.

4. The blowing agent blend of claim 1, wherein the blowing agent blend includes a chemical co-blowing agent.

5. The blowing agent blend of claim 1, wherein the blowing agent blend comprises from about 10 mol % to about 60 mol % isopentane.

6. The blowing agent blend of claim 5, wherein the blowing agent blend comprises from about 15 mol % to about 40 mol % isopentane.

7. The blowing agent blend of claim 6, wherein the blowing agent blend comprises from about 25 mol % to about 40 mol % isopentane.

8. The blowing agent blend of claim 1, wherein the polyolefin foam comprises polyethylene.

9. The blowing agent blend of claim 1, wherein the polyolefin foam has a density of less than 3 lb/ft3.

10. A polyolefin foam structure prepared by the process comprising: melting a thermoplastic polyolefin polymer, dissolving an effective amount of a blowing agent blend in the polyolefin polymer, the blowing agent blend comprising less than about 99 mol % isopentane and at least one co-blowing agent, the co-blowing agent being either a physical co-blowing agent having a boiling point less than 28° C., or a chemical co-blowing agent, or combinations thereof, forming an extrudate, transferring the extrudate to an expansion zone, and permitting the extrudate to expand in the expansion zone to produce the polyolefin foam structure, the polyolefin foam structure being a substantially closed-cell and dimensionally-stable structure.

11. The polyolefin foam structure of claim 10, wherein the extrudate comprises from about 1 to about 18 wt % blowing agent.

12. The polyolefin foam structure of claim 10, wherein the polyolefin foam structure has at least 20 cells per inch.

13. The polyolefin foam structure of claim 12, wherein the polyolefin foam structure has at least 25 cells per inch.

14. The polyolefin foam structure of claim 13, wherein the polyolefin foam structure has at least 30 cells per inch.

15. The polyolefin foam structure of claim 10, wherein the polyolefin foam structure is a sheet.

16. The polyolefin foam structure of claim 10, wherein the polyolefin foam structure is a plank.

17. The polyolefin foam structure of claim 10 further including mixing a nucleating agent and the thermoplastic polyolefin polymer to form a mixture, and dissolving an effective amount of the blowing agent blend into the mixture.

18. The polyolefin foam structure of claim 10 further including: melting a stability control agent, mixing the stability control agent and the thermoplastic polyolefin polymer to form a mixture, and dissolving an effective amount of the blowing agent blend into the mixture.

19. The polyolefin foam structure of claim 10, wherein the polyolefin foam structure comprises polyethylene.

20. The polyolefin foam structure of claim 19, wherein the polyolefin foam structure comprises low density polyethylene.

21. The polyolefin foam structure of claim 10, wherein the polyolefin foam structure has a density of less than 3 lb/ft3.

22. A process for making a polyolefin foam structure comprising: melting a thermoplastic polyolefin polymer, dissolving an effective amount of a blowing agent blend in the polyolefin polymer, the blowing agent blend comprising less than about 99 mol % isopentane and at least one co-blowing agent, the co-blowing agent being either a physical co-blowing agent having a boiling point less than 28° C., or a chemical co-blowing agent, or combinations thereof, forming an extrudate, transferring the extrudate to an expansion zone, and permitting the extrudate to expand in the expansion zone to produce the polyolefin foam structure.

23. The process of claim 22, wherein the polyolefin structure is a substantially closed-cell and dimensionally stable structure.

24. The process of claim 22, wherein the extrudate comprises from about 1 to about 18 wt % blowing agent.

25. The process of claim 22 further including mixing a nucleating agent and the thermoplastic polyolefin polymer to form a mixture, and dissolving an effective amount of the blowing agent blend into the mixture.

26. The process of claim 22 further including: melting a stability control agent, mixing the stability control agent and the thermoplastic polyolefin polymer to form a mixture, and dissolving an effective amount of the blowing agent blend into the mixture.

27. The process of claim 22, wherein the co-blowing agent includes at least one physical co-blowing agent, the at least one physical co-blowing agent being ethane, n-propane, n-butane, isobutane, cyclopropane, nitrogen, argon, carbon dioxide, sulfur hexafluoride, nitrous oxide, dimethyl ether, 1,1-difluoroethane (HFC-152a), 1,1,1-trifluoroethane (HFC-143a), 1,1,1,2-tetrafluoroethane (HFC-134a), 1,1,2,2-tetrafluoroethane (HFC-134), 1,1,1,3,3-pentafluoropropane (HFC-245fa) or combinations thereof.

28. The process of claim 22, wherein the blowing agent blend includes a chemical co-blowing agent.

29. The process of claim 22, wherein the blowing agent blend comprises from about 10 mol % to about 60 mol % isopentane.

30. The process of claim 29, wherein the blowing agent blend comprises from about 15 mol % to about 40 mol % isopentane.

31. The process of claim 30, wherein the blowing agent blend comprises from about 25 mol % to about 40 mol % isopentane.

32. The process of claim 22, wherein the polyolefin foam structure comprises polyethylene.

33. The process of claim 32, wherein the polyolefin foam structure comprises low density polyethylene.

34. The process of claim 22, wherein the polyolefin foam structure has a density of less than 3 lb/ft3.

35. A blowing agent blend for foaming low density polyethylene foam consisting essentially of isopentane and at least one co-blowing agent, the co-blowing agent being either a physical co-blowing agent having a boiling point less than 28° C., or a chemical co-blowing agent, or combinations thereof, and wherein the blowing agent blend includes from about 10 to about 99 mol % isopentane and the remainder consists essentially of the co-blowing agent.

36. The blowing agent blend of claim 35, wherein the co-blowing agent includes at least one physical co-blowing agent, the at least one physical co-blowing agent being ethane, n-propane, n-butane, isobutane, cyclopropane, nitrogen, argon, carbon dioxide, sulfur hexafluoride, nitrous oxide, dimethyl ether, 1,1-difluoroethane (HFC-152a), 1,1,1-trifluoroethane (HFC-143a), 1,1,1,2-tetrafluoroethane (HFC-134a), 1,1,2,2-tetrafluoroethane (HFC-134), 1,1,1,3,3-pentafluoropropane (HFC-245fa) or combinations thereof.

37. The blowing agent blend of claim 35, wherein the blowing agent blend comprises from about 10 mol % to about 60 mol % isopentane.

38. The blowing agent blend of claim 37, wherein the blowing agent blend comprises from about 25 mol % to about 40 mol % isopentane.

39. A process for making a low density polyethylene foam structure prepared by the process comprising: melting a low density polyethylene polymer; dissolving an effective amount of a blowing agent blend in the low density polyethylene polymer, the blowing agent blend comprising from about 10 to about 99 mol % isopentane and at least one co-blowing agent, the co-blowing agent being either a physical co-blowing agent having a boiling point less than 28° C., or a chemical co-blowing agent, or combinations thereof, forming an extrudate, transferring the extrudate to an expansion zone, and permitting the extrudate to expand in the expansion zone to produce the low density polyethylene structure.

40. The process of claim 39 further including: melting a stability control agent, mixing a nucleating agent, the stability control agent and the thermoplastic polyolefin polymer to form a mixture, and dissolving an effective amount of the blowing agent blend into the mixture.

41. The process of claim 40, wherein the nucleating agent is talc, and the stability control agent is glycerol monostearate.

42. The process of claim 39, wherein the co-blowing agent includes at least one physical co-blowing agent, the at least one physical co-blowing agent being ethane, n-propane, n-butane, isobutane, cyclopropane, nitrogen, argon, carbon dioxide, sulfur hexafluoride, nitrous oxide, dimethyl ether, 1,1-difluoroethane (HFC-152a), 1,1,1-trifluoroethane (HFC-143a), 1,1,1,2-tetrafluoroethane (HFC-134a), 1,1,2,2-tetrafluoroethane (HFC-134), 1,1,1,3,3-pentafluoropropane (HFC-245fa) or combinations thereof.

43. The process of claim 39, wherein the blowing agent blend includes a chemical co-blowing agent.

44. The process of claim 39, wherein the blowing agent blend comprises from about 10 mol % to about 60 mol % isopentane.

45. The process of claim 44, wherein the blowing agent blend comprises from about 25 mol % to about 40 mol % isopentane.

46. The process of claim 39, wherein the low density polyethylene foam has a density of less than 3 lb/ft3.

Description:

FIELD OF INVENTION

[0001] The present invention relates generally to foams using blowing agent blends or mixtures, and processes of making the same More particularly, the present invention relates to polyolefin foams using isopentane-based blowing agent blends that produce a stable foam with minimized or no corrugation, and processes of making the same.

BACKGROUND OF THE INVENTION

[0002] Polyolefin foam, such as low density polyethylene foam, is commonly made by combining a physical blowing agent with molten polyethylene resin under pressure and, after thorough mixing, extruding the combination through an appropriate die into a lower pressure atmosphere.

[0003] In the past, physical blowing agents widely used for making polyolefin foams were chlorofluorocarbons and hydrochlorofluorocarbons. Use of such blowing agents, however, has been or will be banned because of environmental concerns.

[0004] Presently, physical blowing agents more commonly used for making low density polyethylene (LDPE) foams are hydrocarbons such as isobutane or blends of isobutane and n-butane. Other hydrocarbons such as ethane and propane have been used more recently in making LDPE foams. The ability of isobutane, n-butane, propane, ethane and combinations thereof to give stable, low density foams depends on factors such as desirable solubility in low density polyethylene, and the ability of gas permeation modifiers to slow down the escape of such blowing agents. The resultant foam article (e.g., a sheet) using such blowing agents is frequently produced with at least some corrugation. Corrugation occurs when the radial rate of expansion is higher than the radial space available for the foam as it exits the die. Corrugation may be reduced to a certain extent by optimizing the foaming process and apparatus used in forming the foam with these blowing agents, but a low degree of corrugation or visible corrugation lanes often remain. The corrugation becomes more pronounced when a fluid with a very low boiling point (e.g., ethane or propane) is (a) used as the sole blowing agent or (b) present in an amount greater than about 5 mol % with a higher boiling fluid (e.g, isobutane). Corrugation also tends to occur more frequently in sheets (thickness of up to about ½ inch) as opposed to planks (thickness of greater than about an inch), and the degree and magnitude of corrugation increase as the foam density decreases.

[0005] Therefore, a need exists for a stable foam having minimized or no corrugation, and a process for making the same.

SUMMARY OF THE INVENTION

[0006] According to one embodiment of the present invention, a blowing agent blend for making polyolefin foams comprises isopentane and at least one co-blowing agent. The co-blowing agent is either a physical co-blowing agent having a boiling point less than 28° C., or a chemical co-blowing agent, or combinations thereof. The blowing agent blend comprises less than about 99 mol % isopentane. The polyolefin foam may be a low density polyethylene foam. The blowing agent blend may consist essentially of isopentane and the co-blowing agent in which the blowing agent blend includes about 10 to about 99 mol % isopentane with the remainder consisting essentially of the co-blowing agent.

[0007] According to another embodiment, a polyolefin foam structure is prepared by the process comprising melting a thermoplastic polyolefin polymer. An effective amount of a blowing agent blend is dissolved in the polyolefin polymer melt. The blowing agent blend comprises less than about 99 mol % isopentane and at least one co-blowing agent. The co-blowing agent is either a physical co-blowing agent having a boiling point less than about 28° C., or a chemical co-blowing agent, or combinations thereof. An extrudate is formed and transferred to an expansion zone. The extrudate is permitted to expand in the expansion zone to produce the polyolefin foam structure that is a substantially closed-cell and dimensionally-stable structure.

[0008] According to a process of the present invention, a polyolefin foam structure is produced that comprises melting a thermoplastic polyolefin polymer. An effective amount of a blowing agent blend is dissolved in the polyolefin polymer melt. The blowing agent blend comprises less than about 99 mol % isopentane and at least one co-blowing agent. The co-blowing agent is either a physical co-blowing agent having a boiling point less than about 28° C., or a chemical co-blowing agent, or combinations thereof. An extrudate is formed and is transferred to an expansion zone. The extrudate is permitted to expand in the expansion zone to produce the polyolefin foam structure. The polyolefin foam structure may comprise a low density polyethylene.

BRIEF DESCRIPTION OF THE DRAWINGS

[0009] FIGURE is a schematic flow diagram of an overall sequence of operations involved in the manufacture of a foamed polyolefin sheet with the blowing agent blends according to one embodiment of the present invention.

[0010] While the invention is susceptible to various modifications and alternative forms, specific embodiments thereof have been shown by way of example in the drawing and will herein be described in detail. It should be understood, however, that it is not intended to limit the invention to the particular forms disclosed but, on the contrary, the intention is to cover all modifications, equivalents, and alternatives falling within the spirit and scope of the invention as defined by the appended claims.

DESCRIPTION OF ILLUSTRATIVE EMBODIMENTS

[0011] Resins that can be foamed in accordance with the present invention include polyolefin resins such as ethylenic polymers and propylenic polymers. Suitable ethylenic polymer materials include ethylenic homopolymers, and copolymers of ethylenic compounds and copolymerizable ethylenically unsaturated comonomers. The ethylenic polymer material may further include minor proportions of non-ethylenic polymers. The ethylenic polymer material may be comprised solely of one or more ethylenic homopolymers, one or more ethylenic copolymers, a blend of one or more of each of ethylenic homopolymers and copolymers, or blends of any of the foregoing with a non-ethylenic polymer. Regardless of composition, the ethylenic polymer material comprises greater than 50 and preferably greater than 70 wt % of ethylenic monomeric units. Most preferably, the ethylenic polymer material is comprised completely of ethylenic monomeric units. Most preferred ethylenic polymers are polyethylene homopolymers. Polyethylenes may be of the high, medium, low, linear low, or ultra-low density type. Most preferred are low density polyethylenes. The polyethylenes may be linear, branched or cross-linked.

[0012] Suitable ethylenic copolymers may be comprised of ethylenic monomeric units and minor amounts, preferably 20 wt % or less, of a monoethylenically unsaturated monomeric unit or units copolymerizable therewith. Suitable comonomers include C1-4 alkyl acids and esters, ionomeric derivatives, C2-6 dienes and C3-9 olefins. Examples of suitable comonomers include acrylic acid, itaconic acid, maleic acid, methacrylic acid, ethacrylic acid, methyl acrylate, methyl methacrylate, ethyl acrylate, vinyl acetate, carbon monoxide, maleic anhydride, acrylonitrile, propylene, isobutylene, and butadiene.

[0013] Polypropylene that may be used in the present invention includes polypropylene homopolymer or copolymers. Various polypropylenes that may be suitable in the present invention include, but are not limited to, atactic, isotactic, syndiotactic, long-chain branched, and propylene/ethylene copolymers.

[0014] The foam processes of the present invention employ a blowing agent blend or mixture to achieve a stable polyolefin foam with minimized or no corrugation. The blowing agent blend used in forming polyolefin foam is isopentane-based. The blowing agents blend comprises at least isopentane and at least one co-blowing agent. The co-blowing agent(s) can be physical, chemical or combinations thereof. The blowing agent blend comprises less than about 99 mol % isopentane.

[0015] A physical co-blowing agent is defined herein as having a boiling point less than 28° C. The co-blowing agent is fast expanding as compared to a pure isopentane blowing agent. The physical blowing agent may be inorganic or organic. Some suitable inorganic blowing agents include, but are not limited to, air, nitrogen, argon, xenon, carbon dioxide, sulfur hexafluoride, nitrous oxide, ammonia, silicon tetrafluoride, nitrogen trifluoride, boron trifluoride, and boron trichloride. Some examples of organic co-blowing agents that may be used in the present invention include, but are not limited to, hydrocarbons, halogenated hydrocarbons, fluids with polar groups, and combinations thereof. Hydrocarbons include, but are not limited to, methane, ethane, propane, cyclopropane, n-butane, isobutane, cyclobutane, and neopentane. Halogenated hydrocarbons include, but are not limited to, methyl fluoride, difluoromethane (HFC-32), trifluoromethane (HFC-23), perfluoromethane, chlorodifluoromethane (HCFC-22), methylene chloride, ethyl chloride, ethyl fluoride, 1,1-difluoroethane (HFC-152a), 1,1,1-trifluoroethane (HFC-143a), 1,1,1,2-tetrafluoroethane (HFC- 134a), 1,1,2,2-tetrafluoroethane (HFC-134), pentafluoroethane (HFC-125), perfluoroethane, 1,1-dichloro-1-fluoroethane (HCFC-141b), 1-chloro-1,1-difluoroethane (HCFC-142b), 1,1 -dichloro-2,2,2-trifluoroethane (HCFC-123), and 1-chloro-1,2,2,2-tetrafluoroethane (HCFC-124), difluoropropane, 1,1,1-trifluoropropane, 1,1,1,3,3-pentafluoropropane (HFC-245fa), perfluoropropane, perfluorobutane, perfluorocyclobutane, and vinyl fluoride. Fluids with polar groups include, but are not limited to, dimethyl ether, vinyl methyl ether, methyl ethyl ether, dimethyl fluoroether, diethyl fluoroether, perfluorotetrahydrofuran, dimethylamine, trimethylamine, ethylamine, and perfluoroacetone.

[0016] Chemical co-blowing agents that may be used include azodicarbonamide, azodilsobutyro-nitrile, benzenesulfonhydrazide, 4,4-oxybenzene sulfonyl-semicarbazide, p-toluene sulfonyl semicarbazide, barium azodicarboxylate, N,N′-dimethyl-N,N′-dinitrosoterephthalamide, trihydrazino triazine, and other azo, N-nitroso, carbonate, and sulfonyl hydrazides. There are also various acid/bicarbonate mixtures that decompose into gases when heated For example, mixtures of citric acid and sodium bicarbonate sold under the name HYDROCEROL® can be employed as chemical co-blowing agents.

[0017] The total amount of the blowing agent blend used depends on conditions such as extrusion-process conditions at mixing, the blowing agent blend being used, the composition of the extrudate, and the desired density of the foamed article. The extrudate is defined herein as including the blowing agent blend, a polyolefin resin(s), and any additives. For a foam having a density of from about 1 to about 15 lb/ft3, the extrudate typically comprises from about 18 to about 1 wt % of blowing agent.

[0018] The blowing agent blend used in the present invention comprises less than about 99 mol % isopentane. The blowing agent blend generally comprises from about 10 mol % to about 60 or 75 mol % isopentane. The blowing agent blend more typically comprises from about 15 mol % to about 40 mol % isopentane. More specifically, the blowing agent blend comprises from about 25 or 30 mol % to about 40 mol % isopentane. The blowing agent blend generally comprises at least about 15 or 30 mol % of co-blowing agent(s). More specifically, the blowing agent blend comprises from about 40 to about 85 or 90 mol % of co-blowing agent(s). The blowing agent blend more typically comprises from about 60 mol % to about 70 or 75 mol % of co-blowing agent(s).

[0019] A nucleating agent or combination of such agents may be employed in the present invention for advantages, such as its capability for regulating cell formation and morphology. A nucleating agent, or cell size control agent, may be any conventional or useful nucleating agent(s). The amount of nucleating agent used depends upon the desired cell size, the selected blowing agent blend, and the desired foam density. The nucleating agent is generally added in amounts from about 0.02 to about 20 wt % of the polyolefin resin composition.

[0020] Some contemplated nucleating agents include inorganic materials (in small particulate form), such as clay, talc, silica, and diatomaceous earth. Other contemplated nucleating agents include organic nucleating agents that decompose or react at the heating temperature within an extruder to evolve gases, such as carbon dioxide and/or nitrogen. One example of an organic nucleating agent is a combination of an alkali metal salt of a polycarboxylic acid with a carbonate or bicarbonate. Some examples of alkali metal salts of a polycarboxylic acid include, but are not limited to, the monosodium salt of 2,3-dihydroxy-butanedioic acid (commonly referred to as sodium hydrogen tartrate), the monopotassium salt of butanedioic acid (commonly referred to as potassium hydrogen succinate), the trisodium and tripotassium salts of 2-hydroxy-1,2,3-propanetricarboxylic acid (commonly referred to as sodium and potassium citrate, respectively), and the disodium salt of ethanedioic acid (commonly referred to as sodium oxalate), or polycarboxylic acid such as 2-hydroxy-1,2,3-propanetricarboxylic acid. Some examples of a carbonate or a bicarbonate include, but are not limited to, sodium carbonate, sodium bicarbonate, potassium carbonate, potassium bicarbonate, and calcium carbonate.

[0021] It is contemplated that mixtures of different nucleating agents may be added in the present invention. Some more desirable nucleating agents include talc, crystalline silica, and a stoichiometric mixture of citric acid and sodium bicarbonate (the stoichiometric mixture having a 1 to 100 percent concentration where the carrier is a suitable polymer such as polyethylene). Talc may be added in a carrier or in a powder form.

[0022] Gas permeation agents or stability control agents may be employed in the present invention to assist in preventing or inhibiting collapsing of the foam. The stability control agents suitable for use in the present invention may include the partial esters of long-chain fatty acids with polyols described in U.S. Pat. No. 3,644,230, saturated higher alkyl amines, saturated higher fatty acid amides, complete esters of higher fatty acids such as those described in U.S. Pat. No. 4,214,054, and combinations thereof described in U.S. Pat. No. 5,750,584.

[0023] The partial esters of fatty acids that may be desired as a stability control agent include the members of the generic class known as surface active agents or surfactants. A preferred class of surfactants includes a partial ester of a fatty acid having 12 to 18 carbon atoms and a polyol having three to six hydroxyl groups. More preferably, the partial esters of a long chain fatty acid with a polyol component of the stability control agent is glycerol monostearate, glycerol distearate or mixtures thereof. It is contemplated that other gas permeation agents or stability control agents may be employed in the present invention to assist in preventing or inhibiting collapsing of the foam.

[0024] If desired, fillers, colorants, light and heat stabilizers, anti-oxidants, acid scavengers, flame retardants, processing aids, extrusion aids and foaming additives may be used in making the foam.

[0025] A conventional two-extruder tandem system with each extruder having a single screw may be used for extruding the foam article of the present invention. Alternatively, a two-extruder tandem system in which the primary extruder is a twin screw, and the secondary extruder is a single screw may be used for extruding the foam article of the present invention. A single extruder with proper cooling may also be employed in the present invention.

[0026] According to one process of the present invention, polyolefin resin pellets (e.g., a low density polyethylene) are admixed with a nucleating agent, such as talc, and a stability control agent, such as glycerol monostearate. These materials are continuously fed into a hopper of an extruder. The feed mixture is conveyed forward by a screw within a barrel of the extruder as the mixture is mixed, compressed, heated, and converted to molten form. The conversion to molten form occurs prior to reaching an injection zone where the blowing agent is added. The blowing agent blend of the present invention may be injected into the polyolefinic composition at a point where the polymer is in a melt state (i.e., beyond the feed zone).

[0027] After injecting the blowing agent blend, the mixture is continuously mixed at pressures to ensure a homogeneous solution of the resin and the blowing agent blend. The molten mixture is then conveyed into a cooling zone where additional mixing takes place. After cooling, the mixture may be extruded into a holding zone maintained at a temperature and pressure that prevents or inhibits foaming of the mixture. The holding zone has (a) an outlet die having an orifice opening into a zone of lower pressure such as atmospheric pressure at which the mixture foams, (b) means for closing the orifice without disturbing the foamable mixture within the holding zone, and (c) opening means for allowing the foamable mixture to be ejected from the holding zone. An example of a holding zone is described in U.S. Pat. No. 4,323,528. Regardless of whether a holding zone is used, the mixture is then extruded through a die into a lower pressure zone, such as atmospheric pressure.

[0028] According to one embodiment, a two-extruder tandem system 10 of the FIGURE may be used for extruding a polyolefin foam article (e.g., a sheet) of the present invention. Polyolefin resin pellets such as polyethylene are mixed with at least one additive (e.g., a nucleating agent and/or stability control agent) to form a feed mixture which is fed continuously into a hopper 11 of a primary extruder 13. The feed mixture is conveyed forward by a helical screw within a barrel of the extruder as the feed mixture is mixed, compressed, heated and melted prior to reaching the blowing agent-injection zone. The blowing agent blend (at least isopentane and one co-blowing agent) is added at point 15. Thus, the blowing agent blend of the present invention is injected into the polyethylene/additives mixture (feed mixture) at a point beyond the feed zone where the polyethylene is melted It is contemplated that the blowing agent blend may be injected at other locations, including into a secondary extruder.

[0029] Following injection of the blowing agent blend, the mixture is continuously mixed in the primary extruder 13. The exit pressure of the primary extruder 13 is generally in the range of from about 1200 to about 2500 psi. The temperature of the primary extruder 13 is generally in the range of from about 300 to about 400° F. The mixture is subsequently passed, at a high enough pressure that the blowing agent blend remains in solution, through a hollow adapter section 17 into a cooled secondary tandem extruder 19. The molten mixture is passed along the length of the cooled secondary extruder at low shear where cooling and additional mixing occur. The exit pressure of the secondary extruder 19 is generally in the range of from about 400 to about 1200 psi. The temperature of the extrudate from the secondary extruder 19 is generally in the range of from about 205 to about 220° F. In general, the temperature of the primary extruder should be sufficient to melt the polymer and any additives, and to promote efficient mixing. The temperature and pressure in the secondary extruder should be sufficient to keep the polymer and the blowing agent blend as a homogeneous solution. The mixture is then expressed through an annular die 21, though a die of a different configuration, such as a flat die, may also be used. The foamable polyethylene polymer is extruded through the annular die 21 in the form of an elongated bubble or tube 23. The foamable polyethylene polymer in the FIGURE is expanded and drawn over a cylindrical surface of a cooling and sizing drum 25, and slit to form sheet stock 27. The sheet stock 27 is taken up on one or more winding reels 29.

[0030] If the article produced is a sheet, the thickness of the sheet can be up to about 0.5 inch. If the article produced is a plank, the thickness is generally greater than about one inch. The articles produced from the extruded tube are generally from about 0.020 to about 0.25 inch in thickness.

[0031] The resulting foamed article generally has a density from about 1 to about 15 lb/ft3, more typically from about 2.0 to about 9.0 lb/ft3. When in sheet form, the foamed article is preferably “low density” which is defined herein as being less than 3 lb/ft3. The resultant foamed article has a substantially closed-cell structure and is defined herein as a foam having greater than about 85% closed cells and, more typically, greater than about 95% closed cells.

[0032] The polyolefin foams are light in weight and may be used as protective or flexible packaging for delicate goods such as computers, glassware, televisions, furniture, and any article that needs to be protected from gouging, surface-scratching or marring. It is contemplated that the polyolefin foams of the present invention may be used in other applications such as floor underlayments, flotation foam (e.g., life jackets), toys and recreational parts. Generally speaking, foam sheets are used in flexible packaging, while foam planks are used in protective packaging. In addition to foam sheets and planks, the present invention may take the form of other shapes such as rods.

[0033] The resulting polyolefin foam of the present invention is preferably “dimensionally stable.” Dimensional stability as defined herein is when the density of the foam does not deviate more than about 15% (i.e., the foam does not either shrink more than about 15% or expand more than about 15%) from the density of the polyolefin foam at the time of production. The density of the polyolefin foam at the time of production refers to its density within about 15 minutes, and preferably within 10 minutes, after the foam exits the die. This measurement is used in determining the “fresh” density-of the foam. To have a dimensionally stable product, the foam is typically measured after an aging process (e.g., for LDPEs from about 5 to about 30 days) and compared to its fresh density. It is recognized, however, that in the unlikely event that the foam at a later duration is not within about 15% of its fresh density, then it is not a dimensionally stable product. It is preferable that the foam does not deviate more than about 10% from its “fresh” density.

[0034] It is desirable for some polyolefin foams of the present invention to have a certain number of cells per inch. For example, it is desirable to have at least 20 or 25 cells per inch, and more preferably 30 cells per inch in both the machine and cross-machine directions for a foam that is about 100 mils thick.

EXAMPLES

[0035] Various blowing agents were tested with the results shown below in Tables 1 and 2. Specifically, several foams were made from comparative blowing agents and inventive blowing agent blends. It should be noted that in the various examples reported in Tables 1 and 2, the hardware was the same and operated in exactly the to same way, the only variable was the blowing agent blend. All of the inventive blowing agent blends included (a) isopentane and (b) either ethane, n-propane, isobutane, butanes (a combination of isobutane and n-butane), 1,1,1,2-tetrafluoroethane (HFC-134a), dimethyl ether, or combinations thereof. The comparative blowing agents did not include isopentane, but rather included either ethane, n-propane, isobutane, butanes (a combination of isobutane and n-butane), HFC-134a, or combinations thereof.

[0036] Each of the foams was made with low density polyethylene (LDPE) having a density of 0.920 g/cm3 and a melt index of 2.0 g/10 min at 190° C. In addition to the blowing agents and the LDPE resin, glycerol monostearate and talc were added in forming the foams. Glycerol monostearate, a stability control agent, was added at a concentration level of about 1 wt % of the total solids, and, talc, a nucleating agent, was added at a concentration level of about 0.1 to 1.0 wt % of total solids. Each of the foam samples, except Inventive Foams 5, 10, and 11, was made on a pilot line. The pilot line is a tandem extrusion line employing 2.5 inch and 3.5 inch single-screw extruders equipped with three ports in the primary extruder for injecting compressed fluids. The foaming temperature used in the pilot line was 107° C. and the foams were produced with a blow-up ratio of either 3.7 or 4.1. The blow-up ratio used to make each foam is identified in the footnotes to Tables 1 and 2 below. The extruded foam tube was stabilized over a mandrel, and then slit to form a sheet.

[0037] Unlike the other foams reported in Tables 1 and 2, Inventive Foams 5, 10 and 11 were made on a miniline. The miniline is a tandem extrusion line employing 1.25 inch and 1.5 inch single-screw extruders. Otherwise, the operating conditions of the miniline were the same as those of the pilot line described above.

[0038] The densities of the resulting foams were measured using ASTM D3575. The corrugation, if any, of the foam was determined as twice the amplitude of the sine wave that rides along the circumference of the extruded tube. The corrugation of the foams made on the miniline (Inventive Foams 5, 10, and 11) was not measured because of the small sample size. 1

TABLE 1 1,2,3
Blowing Agent (Composition in mol %) No. of
Sample No HFC- Density Gage Cells Corrugation
(Comp/Inv)4 Ethane n-C35 134a DME6 i-C47 Butanes8 i-C59 (lbs/ft3) (mils) (Per inch) (mils)
Comp 1 0 0 0 0 0 100 0 20 125 29 50
Comp 2 0 0 0 0 0 100 0 12 128 30 87
Comp 3 0 0 0 0 100 0 0 12 127 28 235
Comp 4 0 0 0 0 100 0 0 2.0 127 30 35
Inv 5 0 0 0 0 35 0 65 18 181 11 NA10
Inv 6 0 0 0 0 0 70 30 14 87 24 0
lnv 7 0 0 0 0 50 0 50 15 78 24 0
lnv 8 0 0 0 0 60 0 40 13 87 24 0
Inv 9 0 0 0 0 68 0 32 20 127 30 0
Inv 10 0 0 15 0 0 0 85 32 130 12 NA
Inv 11 0 0 30 0 0 0 70 35 130 15 NA
Comp 12 0 100 0 0 0 0 0 21 110 28 80
Comp 13 0 100 0 0 0 0 0 12 98 33 107
Inv 14 0 80 0 0 0 0 20 20 98 28 0
Inv 15 0 47 13 0 0 0 40 12 98 28 40
Inv 16 0 15 0 0 70 0 15 22 123 30 0
Inv 17 0 7 0 0 68 0 25 20 127 30 0
Inv 18 0 14 0 0 66 0 20 20 125 30 0
1Comparative Samples 1, 2, 12 and 13, and Inventive Samples 6-8 and 14-15 were made on the pilot line with a blow-up ratio of 4 1
2Comparative Samples 3 and 4, and Inventive Samples 9 and 16-18 were made on the pilot line with a blow-up ratio of 3 7
3Inventive Samples 5, 10 and 11 were made on the miniline with a blow-up ratio of 3
4“Comp” = Comparative Sample, “Inv” = Inventive Sample
5n-C3 = n-propane
6DME = Dimethyl ether
7i-C4 = Isobutane
8Butanes = A blend of 65 mol % isobutane and 35 mol % n-butane, generally known as A26
9i-C5 = Isopentane
10NA = Not Available

[0039] All of the above foams of Table 1 were dimensionally stable because their density did not deviate more than about 15% as compared to the foam density at the time of production. It was generally observed that the level of corrugation of the foam increased as the relative amount of isopentane was reduced or the relative amount of the co-blowing agent was increased.

[0040] Specifically, the corrugation of Comparative Foams 1-4 (a blowing agent of either isobutane or butanes) was greater than the corrugation of Inventive Foams 6-9 (a blowing agent of isopentane with either isobutane or butanes). Compare corrugation levels of 35-235 mils of Comparative Foams 1-4 to 0 mil of Inventive Foams 6-9. Similarly, the corrugation of Comparative Foams 12-13 (a blowing agent of n-propane) was greater than the corrugation of Inventive Foam 14 (a blowing agent of 80 mol % n-propane and 20 mol % isopentane). Compare corrugation levels of 80 and 107 mils of Comparative Foams 12 and 13, respectively, and 0 mil of Inventive Foam 14. It was surprising that the corrugation levels of Inventive Foams 6, 7-9 and 14 decreased significantly as compared to the corrugation levels of Comparative Foams 1-2, 3-4, and 12-13, respectively, by replacing a portion of the butanes, isobutane or n-propane with isopentane. 2

TABLE 21,2
Blowing Agent (Compostion in mol %) No of
Sample No. HFC Density Gage Cells Corrugation
(Comp/Inv)3 Ethane n-C34 134a DME5 i-C46 Butanes i-C58 (lbs/ft3) (mils) (Per inch) (mils)
Comp 19 10 0 0 0 90 0 0 20 102 28 100
Inv 20 10 0 0 0 65 0 25 20 96 28 80
Comp 21 25 0 0 0 75 0 0 20 102 30 75
Inv 22 25 0 0 0 45 0 30 21 94 30 60
Comp 23 40 0 0 0 60 0 0 20 96 28 60
Inv 24 40 0 0 0 30 0 30 21 95 28 60
Comp 25 0 0 15 0 85 0 0 12 87 40 73
Inv 26 0 0 15 0 70 0 15 19 123 30 0
Inv 27 0 0 13 0 0 57 30 13 108 26 42
Inv 28 0 0 0 15 70 0 15 12 127 30 167
Inv 29 0 0 0 15 70 0 15 19 118 30 105
Inv 30 0 0 0 7 68 0 25 20 125 30 0
Inv 31 0 0 0 14 57 0 29 20 122 29 0
Inv 32 0 0 0 13 66 0 21 21 128 29 0
1Comparative Sample 25 and Inventive Sample 27 were made on the pilot line wtth a blow up ratio of 4 1
2Comparative Samples 19, 21, and 23 and Inventive Samples 20, 22, 24, 26, and 28-32 were made on the pilot line with a blow up ratio of 3 7
3“Comp” = Comparative Sample, “Inv” = Inventive Sample
4n-C3 = n-propane
5DME = Dimethyl ether
6i-C4 = Isobutane
7Butanes = A blend of 65 mol % and 35 mol % n-butane, generally known as A26
8i-C5 = Isopentane

[0041] All of the above foams of Table 2 were dimensionally stable because their density did not deviate more than about 15% as compared to the density of the foam at the time of production. It was generally observed that the level of corrugation of the foam increased as the relative amount of isopentane was reduced or the relative amount of the volatile blowing agent was increased, as demonstrated in Inventive Foams 29 and 31. Specifically, the corrugation of Comparative Foam 19 (a blowing agent of 10 mol % ethane and 90 mol % isobutane) was greater than the corrugation of Inventive Foam 20 which replaced some of the isobutane with isopentane. Compare corrugation levels of 100 mils of Comparative Foam 19, and 80 mils of Inventive Foam 20. Similarly, the corrugation of Comparative Foam 21 (a blowing agent of 25 mol % ethane and 75 mol % isobutane) was slightly greater than the corrugation of Inventive Foam 22 in which some of the isobutane was replaced by isopentane. Compare 75 mils of Comparative Foam 21, and 60 mils of Inventive Foam. Additionally, the corrugation of Comparative Foam 25 (a blowing agent of isobutane and HFC-134a) was greater than the corrugation of Inventive Foam 26 which replaced some of the isobutane with isopentane. Compare corrugation levels of 73 mils of Comparative Foam 25, and 0 mil of Inventive Foam 26. It was surprising that the corrugation levels of Inventive Foams 20, 22 and 26 were less than the corrugation levels of Comparative Foams 19, 21, and 25, respectively, by replacing a portion of the isobutane with isopentane.

[0042] While the present invention has been described with reference to one or more particular embodiments, those skilled in the art will recognize that many changes may be made thereto without departing from the spirit and scope of the present invention. Each of these embodiments and obvious variations thereof is contemplated as falling within the spirit and scope of the claimed invention, which is set forth in the following claims.

What is polyolefin?
A polyolefin is a type of polymer with the general formulaₙ where R is an alkyl group. They are usually derived from a small set of simple olefins. Dominant in a commercial sense are polyethylene and polypropylene. More specialized polyolefins include polyisobutylene and polymethylpentene. They are all colorless or white oils or solids. Many copolymers are known, such as polybutene, which derives from a mixture of different butene isomers. The name of each polyolefin indicates the olefin from which it is prepared; for example, polyethylene is derived from ethylene, and polymethylpentene is derived from 4-methyl-1-pentene. Polyolefins are not olefins themselves because the double bond of each olefin monomer is opened in order to form the polymer. Monomers having more than one double bond such as butadiene and isoprene yield polymers that contain double bonds and are usually not considered polyolefins. Polyolefins are the foundations of many chemical industries.

How are polyolefins made?
The major processes for polyolefins’ production using Ziegler–Natta catalysts involve polymerization in the gas phase or in slurry, including bulk liquid monomer in the case of propylene. LLDPE is also produced via a solution process operating at temperatures in the range 130–250 °C. Polyolefins are produced using refined metallocene catalysts that have a constrained transition metal (generally a Group 4B metal such as Ti, Zr, or Hf) sandwiched between one or more cyclopentadienyl ring structures to form a sterically hindered polymerization site. Polyolefins, also called polyalkenes, are the largest class of commodity thermoplastics. They are polymers of simple alkenes such as ethylene, propylene, butenes, and pentenes, and copolymers thereof. The two most important polyolefins are polyethylene (PE) and polypropylene (PP).

What was the production of polyolefins in 2000?
Polyolefin fibre production by year 2000 was over 1.45 Mt (3.18 billion lb), while the polyester total was 1.76 Mt (3.87 billion lb).

How big is the global market for polyolefins?
Presently, the total world polyolefins capacity exceeds 120 million tons per year. Polyethylene (i.e., HDPE, LDPE and LLDPE) and polypropylene cover 60 % and 40 % of the total polyolefins production, respectively. The annual world-wide polyolefins market growth in the coming years is foreseen to be 4-6%.

What are the industrial applications of polyolefin fibres?
Polyolefin fibres, in particular slit films and monofilament, are used in industrial applications to manufacture ropes, cordages, agricultural nets, and FIBCs (flexible intermediate bulk containers).

Major Manufacturers of Polyolefin and Suppliers of Polyolefin in the World

  • LG Chem Ltd.
  • Constab Polyolefin Additives GmbH
  • Mc Tohcello (Malaysia) Sdn Bhd
  • Dow Europe GmbH
  • SK Chemicals
  • Deutsche Infineum GmbH
  • Bagla Polifilms Ltd.
  • Siam Synthetic Latex Co., Ltd.
  • Hoyer France
  • Lubrizol France

TOP 40 POLYOLEFIN PRODUCERS (POLYPROPYLENE, POLYETHYLENE & COPOLYMERS)

  • Alpek
  • Arkema
  • Borealis Group
  • Borouge
  • Braskem
  • Chevron-Phillips
  • CNPC
  • Dow
  • DuPont
  • Eastman
  • ENI
  • ExxonMobile
  • Formosa Plastics
  • Hanwha
  • Indorama
  • Ineos
  • KAP
  • Kayavlon Impex
  • LCY Chemical
  • LG Chem
  • Lyondellbasell
  • Mitsubishi
  • Mitsui Chemicals
  • Mol Group
  • Nova Chemicals
  • Petkim
  • Petroquim
  • Polyone
  • Quenos
  • Reliance
  • Repsol
  • Sabic
  • Sasol
  • Saudi Polymers
  • SCG Chemical
  • SEPC
  • Sibur
  • Sinopec
  • Sipchem
  • SK Global Chemical
  • Sumitomo
  • Tosoh
  • Total
  • TPC
  • UBE Industries
  • Westlake

Pentane, Hexane and Heptane Prices, Upstream, Downstream, Analytics & Forecasts
Junyuan Petroleum GroupDongying Liangxin Petrochemical Technology Development Limited Company | Address: No. 117, Guangqing Rd., Guangrao County, Dongying 257345 China.
Junyuan Petroleum Group is China’s largest manufacturer of blowing agents to the foam insulation markets. We have continued to grow with the development of next generation blowing agents, offering a variety of hydrocarbon products for the PIR, PUR and EPS markets, available in ISO tanks and drums. For more information, or for pricing please contact us: +86 178 1030 0898 Email: info@junyuanpetroleumgroup.com Web: www.junyuanpetroleumgroup.com.
China is the world’s largest buyer and drives prices in Asia and the global solvent trade. Our comprehensive news and pricing coverage of China and global solvent market is constantly updated by our raw material purchase, production and sales team of experts. Solvent markets can react to change quickly. It’s crucial for buyers, sellers and producers to stay alert and aware of what’s happening, both in their region and internationally. We help you stay abreast of change as it’s happening. We keep you informed of the current price and market position, so you can make the most of opportunities to trade or secure a deal.

Cyclopentane: a new blowing agent for polyurethane foam

Cyclopentane is used as a new blowing agent for rigid polyurethane foam. Now it has been widely used in fluorine-free refrigerator, freezer industry, cold storage, pipeline insulation and other fields. In the future, cyclopentane will become the leading role in the field of polyurethane blowing agent. Dongying Liangxin Petrochemical Technology Development Limited Company will tell you about the control points of cyclopentane in the foaming process.

  1. Strictly control the physical and chemical properties of stock solution
    The chemical properties of polyisocyanate, combined polyether, foaming agent, catalyst and foam stabilizer in black and white materials directly determine the chemical reaction of polyurethane synthesis and the physical properties of foam. It is the basic condition for producing qualified polyurethane foam.
    Black and white monomers shall be transparent viscous liquid without flocculent insoluble impurities. If there are insoluble impurities, the filter screen of the foaming machine will be blocked, resulting in unstable raw material flow, the ratio of black and white materials does not meet the requirements, and the mixture is uneven. Even the pipeline of the foaming machine is blocked.
    It is recommended to thoroughly clean the black and white material filter screens and needle valves of the foaming machine (and premixer) at least once a week.
  2. Strictly control the proportion and injection volume of stock solution
    The proportion of black material, combined polyether and cyclopentane must be strictly controlled. When the total injection volume remains the same, if the proportion of black material is too large, bubbles will appear, if the proportion of white material is too large, soft bubbles will appear, if the proportion of cyclopentane is too large, bubbles will appear, and if the proportion is too small, bubbles will appear. If the proportion of black and white materials is out of balance, the mixture will be uneven and the foam will shrink.
    The injection volume shall be subject to the process requirements. When the injection volume is lower than the process requirement, the foam molding density and strength will be low, and even the filling will not be dense. When the injection volume is higher than the process requirements, bubble expansion and bubble leakage will occur, and the box (door) will be deformed.
  3. Strictly control the process temperature and curing time
    Polyurethane foaming is a complex physical and chemical reaction process. The fluctuation of raw material, mold, preheating temperature and curing time will directly affect the foaming quality.
    A. Black material is a kind of active chemical substance, which is easy to react with water. During storage, the container shall be dry and sealed and filled with dry nitrogen for protection. It shall not be in direct contact with water during use. If the storage temperature is lower than 5 ℃, crystallization will occur, so attention must be paid to antifreeze. Once crystallization occurs, it shall be heated and melted at 70~80 ℃ before use, and fully stirred. When the storage temperature is higher than 50 ℃, an insoluble solid will be produced, the viscosity will increase and the chemical properties will change. White materials have the same properties.
    Therefore, black and white materials shall be stored in a ventilated, cool and dry place at room temperature (20~25 ℃) to avoid sun and rain.
    B. The black and white materials shall be subject to constant temperature treatment before foaming, and the foaming temperature shall be controlled at 18~25 ℃.
    When the temperature is too low, the black and white materials have high viscosity, unstable flow, poor fluidity and uneven mixing. When the temperature is too low, the reaction speed of forming foam is slow and the curing time is long. When the curing time is not enough, the box and door are still foaming after demoulding, resulting in appearance deformation.
    When the temperature is too high, the reaction is violent and difficult to control. It is easy to see that the performance of the foam injected into a large box is uneven. The foam injected at the beginning has undergone a chemical reaction, and the viscosity increases rapidly. The foam injected later has not yet reacted. As a result, the foam liquid injected later cannot push the foam liquid injected first to the front of the foaming process of the box, resulting in local cavitation in the box.
    C. The preheating furnace temperature shall be controlled at 30~50 ℃, the foaming furnace temperature shall be controlled at 35~50 ℃, and the foaming mold temperature shall be controlled at 35~45 ℃.
    The temperature of the box and door to be foamed in winter is low, so it must be preheated in the preheating furnace. Otherwise, when the hot polyurethane liquid contacts the box or door body, the chemical reaction will be seriously affected, and the foam liquid will not stick to the shell.
    When the temperature of the foaming mold is too low, the fluidity of the foaming solution system is poor, the curing time is long, the reaction is not complete, and cavitation occurs; When the temperature of the foaming mold is too high, the plastic liner is deformed by heating, and the foam system reacts violently. Therefore, the temperature of the foaming mold and the ambient temperature of the foaming furnace must be strictly controlled.
    Especially in winter, the foaming mold, preheating furnace, foaming furnace, box and door must be preheated for more than 30 minutes every morning when the line is opened. After a period of foaming in summer, the foaming system must be cooled.
    D. The foaming and curing time of black and white materials used by our company must be more than 6 minutes. The curing time is too short, and the box and door are still foaming after demoulding, resulting in appearance deformation. In particular, after the door body is deformed, the door seal gap is large when it is assembled with the box, the cold leakage occurs, the box is not insulated, and the compressor is frequently started.
  4. Strictly control the injection pressure of foaming machine at 13~16mpa
    When the injection pressure is unstable, the proportion of black and white materials is unstable and the mixing is insufficient. The injection pressure difference between black and white materials shall be controlled within 5bar, otherwise the foaming machine will be damaged due to material mixing.
    During the foaming process, the injection pressure of the foaming machine shall be checked frequently, and the injection system of the foaming machine shall be cleaned to avoid blocking.
    Black, white and cyclopentane are mixed unevenly, which is manifested by uneven density of polyurethane foam, local large bubbles, cracking of foam and local softening of foam: white, yellow or black stripes appear on foam, and foam shrinks.
  5. Preparation before foaming:
    A. Clean and inspect the mold. Before foaming, clean up the missing foam and other debris attached to the foaming mold, and check the mold fitting accuracy. Otherwise, serious quality problems such as damage to the box and bubble leakage will occur during foaming. Before foaming, check whether the exhaust and suction pipes of the box are well arranged as required and whether there are bends. Whether the outgoing line is complete and whether the drainage pipe has been installed. Whether the foaming process board is properly pasted according to the process requirements.
    B. Before door foaming, check whether the handle of the door body is installed correctly and whether it is inclined. Whether the wiring assembly dimension meets the process requirements. Whether the door lock is assembled as required. Whether the masking paper is pasted according to the process requirements and whether there is possibility of bubble leakage.
  6. Requirements for taking and placing box (door) body:
    The (door) body shall be handled vertically and gently, and no damage to the inner and outer boxes is allowed; The foamed box (door) shall be placed on the assembly line at uniform intervals. Then check whether the foaming quality meets the requirements. The leaking bubble shall be cleaned with tools, and the box (door) shall not be scratched.
  7. Foaming process control method
    1) Before each shift of production, it is necessary to check whether the parameters meet the process requirements. Check again every 3 hours and record the inspection results.
    2) Before each shift of production, the mixing condition and density of free foam must be tested. The mixing condition and density of the molded foam of the box body and the door body shall be tested once a shift. Then the free foam and molded foam were frozen at -20 ℃ for 24h, and their shrinkage was observed. The foam body shall have no obvious shrinkage. And record the inspection results.
    The above are the control points of cyclopentane in the foaming process. I hope it will help you. Please consult us for more questions about cyclopentane!
Cyclopentane for rigid polyurethane foam manufactured by Junyuan Petroleum Group
yclopentane manufactured by Junyuan Petroleum Group
Manufacturing base for Cyclopentane used for production of rigid polyurethane foam

Cyclopentane used as in the production of polyurethane insulating foam

Cyclopentane, 95%, Junyuan Petroleum Group
Specifications 

Synonyms: Pentamethylene , ciclopentano, cyclopentan, zyklopentan, unii-t86pb90rnu, hsdb 62, t86pb90rnu, cyclopentanes, cyclopentyl group, hydrocarbons, cyclic c5 and c6

InChI Key : RGSFGYAAUTVSQA-UHFFFAOYSA-N
Formula: C₅H₁₀
MW: 70.13 g/mol
Melting Pt: –95 °C
Density: 0.748
Storage Temperature: Ambient
MDL Number: MFCD00001356
CAS Number: 287-92-3
EINECS: 206-016-6
UN: 1146
ADR: “3”,II
IUPAC Name : Cyclopentane 
SMILES : C1CCCC1
Melting Point: °C to 95°C
Boiling Point: 47°C to 49°C
Flash Point: -37°C (-34°F)
Assay Percent Range: 95%
UN Number: UN1146
Beilstein: 1900195
Merck Index: 14,2741
Refractive Index: 1.406
Quantity: 20 MT/ISO Tank, 150kg/steel drum
Solubility Information: Miscible with ethanol,ether and acetone. Slightly miscible with water.
Formula Weight: 70.14
Physical Form: Liquid
Percent Purity: 95%
Chemical Name or Material: Cyclopentane
 
Description
Cyclopentane is used as green blowing agent and involved in the production of polyurethane insulating foam, which is used in refrigerators, freezers, water heaters, construction panels, insulated pipes and roofs. As a lubricant, it finds applications in computer hard drives and outer space equipment due to its low volatile nature. It is widely useful in the preparation of resin, adhesives and pharmaceutical intermediate. It is an additive in gasoline. Since it is a halogen free compound and has zero-ozone depletion potential, it replaces the conventionally used chloro fluoro carbon (CFC) in refrigeration and thermal insulation.
This Thermo Scientific brand product was originally part of the Alfa Aesar product portfolio. Some documentation and label information may refer to the legacy brand. The original Alfa Aesar product / item code or SKU reference has not changed as a part of the brand transition to Thermo Scientific.
Applications
Cyclopentane is used as green blowing agent and involved in the production of polyurethane insulating foam, which is used in refrigerators, freezers, water heaters, construction panels, insulated pipes and roofs. As a lubricant, it finds applications in computer hard drives and outer space equipment due to its low volatile nature. It is widely useful in the preparation of resin, adhesives and pharmaceutical intermediate. It is an additive in gasoline. Since it is a halogen free compound and has zero-ozone depletion potential, it replaces the conventionally used chloro fluoro carbon (CFC) in refrigeration and thermal insulation.
Solubility
Miscible with ethanol, ether and acetone. Slightly miscible with water.
Notes
Avoid heat, direct sunlight, flames and sparks. Incompatible with strong oxidizing agents.
 
Safety and Handling
GHS H Statement
H225
P210-P233-P235-P240-P241-P242-P243-P261-P271-P280-P301+P310-P303+P361+P353-P304+P340-P312-P331-P370+P378q-P501c
H225-H304-H335-H336
DOTInformation : Transport Hazard Class: 3; Packing Group: II; Proper Shipping Name: CYCLOPENTANE
EINECSNumber : 206-016-6
RTECSNumber : GY2390000
TSCA : Yes
Recommended Storage : Ambient temperatures

ISO 22K2 20-ft foodgrade n-Hexane tank containers

ISO Code 22K2 foodstuff tank containers.

Dimensions: Length 6,058 millimeters (20 feet), Height 2,591 millimeters (8 feet 6 inches), Width 2,438 millimeters (8 feet).
Tank specifications: Minimum pressure 255 kilopascal (2.65 bar, 38.43 pounds per square inch).

If the customers arrange to rent an ISO tank, what are our requirements for the tank container?

Factory address: No. 117, Guangqing Road, Guangrao County, Dongying, Shandong
Add: No. 117, Guangqing Rd., Guangrao County, Dongying China
ISO tank container requirements: (with emergency shut-off valve and meteorological interface, pressure gauge, super gasket, explosion-proof disc, three kilogram air tightness test, 0.5 pound nitrogen pressure maintaining)
ISO tank requirements: (with emergency shut-off valve and meteorological interface, pressure gauge, super gasket, explosion-proof piece, 3kg air tightness test, 0.5lb nitrogen pressure maintaining)

2-Methylbutane

2-Methylbutane

2-Methylbutane MSDS (material safety data sheet) or SDS, CoA and CoQ, dossiers, brochures and other available documents.

  • SDS
  • CoA

Synonyms: iso-Pentane, Isopentane

CAS #: 78-78-4 
EC Number: 201-142-8 
Molar Mass: 72.15 g/mol 
Chemical Formula: C5H12 
Hill Formula: C₅H₁₂

TDS-Isopentane

We have the highest-quality isopentane, pentane, cyclopentane, petroleum ether, Isohexane and n-Heptane.

Key Specification Table

CAS #EC NumberHill FormulaChemical FormulaMolar Mass
78-78-4201-142-8C₅H₁₂C5H1272.15 g/mol

2-Methylbutane Chemical Properties,Uses,Production

Chemical Properties

2-Methylbutane (isopentane), C5H12, is a flammable liquid and exhibits physical properties very similar to those of pentane. It has been detected in urban air.

2-Methylbutane is an alkane that is butane substituted by a methyl group at position 2.  It has a higher BP than butane because, although similarly branched, it has a higher MW. A useful analogy for comparing molecules with the same size of longest chain is that of cylindrical-shaped molecules. It has a role as a refrigerant. Biological samples flash frozen for example with a combination of liquid nitrogen and methylbutane can then be used for storage, cryosection, etc.

Physical properties

Clear, colorless, watery, very flammable liquid with a pleasant odor. Evaporates quickly when spilled. An odor threshold concentration of 1.3 ppmv was reported by Nagata and Takeuchi (1990).

Uses

Isopentane is an organic, branched-chain alkane with five carbon atoms. 2-Methylbutane undergoes catalytic dehydrogenation in the presence of chromia-alumina catalyst to form isoamylenes, which can undergo further dehydrogenation to form isoprene. It may also be used as a solvent in the preparation of trans-Bis(triethylphosphine) (hydroxy carbonyl) (phenyl) platinum(II), a metallacarboxylic acid.

Uses

2-Methylbutane is used as a chemical intermediate. It acts as a blowing agent for polystyrene and gasoline additive. It is used as a solvent of polyethylene and involved in the preparation of polystyrene foam and polyurethane foam. Further, it is used in a closed loop in geothermal power production to operate turbines. In addition to this, it is used to freeze biological samples like tissues in place of dry ice for cryosectioning in histology.

Uses

Solvent, manufacture of chlorinated derivatives, blowing agent for polystyrene.

Definition

ChEBI: An alkane that is butane substituted by a methyl group at position 2.

Production Methods

Isopentane is produced by fractional distillation of natural gas liquids and crude oil.

General Description

Watery colorless liquid with a gasoline-like odor. Floats on water. Flammable, irritating vapor is produced. Boiling point is 82°F.

Air & Water Reactions

Highly flammable. Insoluble in water.

Reactivity Profile

2-Methylbutane is a fire and explosion hazard when in contact with oxidizing agents. .

Hazard

Highly flammable, dangerous fire risk.

Health Hazard

Inhalation causes irritation of respiratory tract, cough, mild depression, irregular heartbeat. Aspiration causes severe lung irritation, coughing, pulmonary edema; excitement followed by depression. Ingestion causes nausea, vomiting, swelling of abdomen, headache, depression.

Fire Hazard

Behavior in Fire: Highly volatile liquid. Vapors may explode when mixed with air.

Safety Profile

Mddly toxic and narcotic by inhalation. See also PENTANE. Flammable liquid. A very dangerous fire and explosion hazard when exposed to heat, flame, or oxidzers. Keep away from sparks, heat, or open flame; can react with oxidizing materials. To fight fire, use foam, CO2, dry chemical. When heated to decomposition it emits acrid smoke and irritating fumes.

Source

A constituent in gasoline. Harley et al. (2000) analyzed the headspace vapors of three grades of unleaded gasoline where ethanol was added to replace methyl tert-butyl ether. The gasoline vapor concentrations of 2-methylbutane in the headspace were 24.1 wt % for regular grade, 24.8 wt % for mid-grade, and 26.0 wt % for premium grade.
Schauer et al. (2001) measured organic compound emission rates for volatile organic compounds, gas-phase semi-volatile organic compounds, and particle-phase organic compounds from the residential (fireplace) combustion of pine, oak, and eucalyptus. The gas-phase emission rate of 2-methylbutane was 5.6 mg/kg of pine burned. Emission rates of 2-methylbutane were not measured during the combustion of oak and eucalyptus.
California Phase II reformulated gasoline contained 2-methylbutane at a concentration of 79.2g/kg. Gas-phase tailpipe emission rates from gasoline-powered automobiles with and without catalytic converters were 3.69 and 148 μg/km, respectively (Schauer et al., 2002).

Environmental Fate

Photolytic. When synthetic air containing gaseous nitrous acid and 2-methylbutane was exposed to artificial sunlight (λ = 300–450 nm), acetone, acetaldehyde, methyl nitrate, peroxy-acetal nitrate, propyl nitrate, and pentyl nitrate were formed (Cox et al., 1980).
Based upon a photooxidation rate constant of 3.90 x 10-12 cm3/molecule?sec with OH radicals in summer daylight, the atmospheric lifetime is 36 h (Altshuller, 1991). At atmospheric pressure and 300 K, Darnall et al. (1978) reported a rate constant of 3.78 x 10-12 cm3/molecule?sec for the same reaction.
Cox et al. (1980) reported a rate constant of 5.0 x 10-11 cm3/molecule?sec for the reaction of gaseous 2-methylbutane with OH radicals based on a value of 8 x 10-12 cm3/molecule?sec for the reaction of ethylene with OH radicals.
Chemical/Physical. Complete combustion in air produces carbon dioxide and water vapor.
2-Methylbutane will not hydrolyze because it does not contain a hydrolyzable functional group.

Purification Methods

Stir isopentane for several hours in the cold with conc H2SO4 (to remove olefinic impurities), then wash it with H2O, aqueous Na2CO3 and H2O again. Dry it with MgSO4 and fractionally distil it using a Todd column packed with glass helices. Material transparent down to 180nm is obtained by distilling from sodium wire, and passing through a column of silica gel which had previously been dried in place at 350o for 12hours before use. [Potts J Phys Chem 20 809 1952, Beilstein 1 IV 320.]

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