Tag normal pentane

Oil Production by Hexane Solvent Extraction

Oil Production by Hexane Solvent Extraction

Solvent extraction consists of a sequence of four operations:
(1) physical removal of oil from the seed in the extractor;
(2) desolventizing-toasting of the de-oiled seeds, often combined with drying and cooling of the meal;
(3) distillation to remove the solvent from the extracted oil;
(4) recovery of the solvent, for reuse in the extractor. The solvent is almost always hexane, which satisfies the technical, economical, and operational needs of all oil millers. Several other solvents have been studied but their disadvantages are such that they cannot compete with hexane, which has many compensatory advantages despite being flammable (Dijkstra and Segers 2007).

The industry generally makes a distinction between two types of extractor: percolation type and immersion type. The percolation process, also known as the continuous extraction process, is based upon the principle of uninterrupted passage of the solvent through the bed of oleaginous material; the oil is thus dissolved in the solvent and carried away. In the immersion process, the entire load of seeds is immersed in solvent. The system is static, so it needs to be stirred to balance the differences in the oil–solvent concentration. Stirring inevitably causes abrasion of the extraction material, so the mixture needs subsequently to be filtered out. This method is used when it is not easy to extract the oil from the matrix. Oil extractors can also be classified on the basis of other different criteria, such as basket or belt operation, rotary or straight, or other shapes, full or partial countercurrent operation, etc.; however, it must be underlined that today the systems available in the market are becoming more and more similar to each other (Fils 2000). The oil-saturated solvent obtained from the extraction process is referred as “miscella.” All commercial extractors are today based on the principle of countercurrent extraction. Fresh solvent encounters previously extracted material, whereas new seeds, flakes, or collet encounter solvent already containing some oil. This method is able to remove a high level of oil using a little solvent quantity (Anderson 2011). Temperature is one of the key variables to keep under control and to optimize the extraction process. The boiling point of hexane is about 69°C near ambient pressure. However, it becomes an azeotrope in the presence of water or steam, with a boiling temperature of 61.6°C. It would be desirable to operate close to the temperature point of this azeotrope; it is the hottest temperature reachable before hexane evaporation, thus it would allow to obtain the lowest viscosity of both solvent and oil and consequently to promote a rapid oil solubilization (Anderson 2011). The length of the extraction process is determined by several factors that affect the contact time between the solvent and the oleaginous material, required for a best extraction yield. Among these factors, the oil concentration, the viscosity of solvent and oil, the shape and size of solid particles and their resulting specific internal structure after pretreatment, are essential to calculate the residence time of the solvent in the extractor. Simulations reported that the greatest amount of oil is extracted during the first minutes, being the oil less accessible to the solvent in the last phase due to equilibrium phenomena (Anderson 2011).

After oil extraction, the meal contains 25%–35% of solvent, which must be evaporated and recovered for reuse (Nagaraj 2009). On the other hand, the de-oiled meal is toasted to reduce anti-nutritional factors such as glucosinolates or trypsin inhibitors, which act as antigrowth factors in monogastric animals if the meal is incorporated into animal feed. Moreover, the meal should be dried to minimize the risk of biological contamination and cooled close to room temperature to remain flowable during storage and transport. The process known as desolventizing, toasting, drying and cooling process (DTDC), invented by Schumacher (1985), combine all these operations in a single piece of equipment (Kemper 2011). The most widely used equipment today is the vertical stack consisting of a number of chambers separated by trays. The meal enters at the top and is conveyed downward while being mixed by agitating sweeps anchored to a central rotating shaft. The heat needed for increasing meal temperature and evaporating the solvent is supplied by steam, which is directly and indirectly introduced into the meal via the trays. When indirectly heated using a steam jacket, hexane will evaporate and the temperature will not rise above the boiling point of hexane. Moreover, in this way, live steam will not condense on the flakes, thus allowing a control of the moisture level during the next steps. The reduced moisture, however, provides less protection against overheating, which may lead to a significant decline of the nutritional value during toasting. Subsequently, the material is heated with live steam, which will condense and raise the temperature above the boiling point of hexane that will be completely vaporized. Additionally, the condensed steam humidifies the meal to a point where a good toasting is possible. In the next chamber, the desolventized meal is cooled and dried by air. Heated air is passed over the material to dry it, at the same time, outside air is blown through the material to cool it. Furthermore, the hot air, while drying, also cools the material and the cold air, while cooling, also dries the material (Kemper 2011).

The miscella leaves the extractor with a 25%–30% oil content, which is separated from the solvent by evaporation of the latter. The miscella evaporator, also referred to as economizer, utilizes the latent heat contained in the vapors leaving the desolventizer to evaporate the solvent till an oil concentration of 65%–75%. The concentrated miscella may then undergo to a second step of solvent evaporation, which utilizes the sensible heat of the condensate steam coming from the DTDC. The residual hexane is then removed by vacuum stripping. The evaporated solvent must be cooled in a condenser and cleaned into a mineral absorption system before being reused in the extractor (Dijkstra and Segers 2007).

Junyuan Petroleum Group donated money to help Heze fight epidemic

Junyuan Petroleum Group donated money to help Heze fight epidemic

The epidemic situation is merciless, but people are sentient and work together to tide over the difficulties. In August, the situation of epidemic prevention and control in Heze City was extremely severe. In order to help Heze City win the sniper battle of epidemic prevention and control, on August 2, Junyuan Petroleum Group, the parent company of Dongying Liangxin Petrochemical Technology Development Limited Company actively supported Heze City and donated 50,000 yuan to the Red Cross Society of Heze City for the prevention and control of COVID-19 epidemic in Caoxian county and Mudan District. It practiced the responsibilities and responsibilities of private enterprises with practical actions, and gathered the positive energy of working together to overcome difficulties.

In recent years, Junyuan Petroleum Group, the parent company of Dongying Liangxin Petrochemical Technology Development Limited Company, has made positive contributions to social welfare undertakings while achieving rapid development. Participated in the educational activities organized by Dongying Civil Affairs Bureau, and donated 100,000 yuan at one time; Participated in the targeted poverty alleviation and Charity Day donation activities in Dingzhuang Town, Guangrao County, and donated 130,000 yuan; In response to the targeted poverty alleviation activities of Guangrao County Charity Federation, donated 200,000 yuan; In the year of COVID-19, the company donated 500000 yuan to Dingzhuang sub district Charity Federation and donated prevention and control materials to surrounding villages and epidemic prevention and control points under the condition that its production and operation were seriously affected.

Next, Junyuan Petroleum Group, Dongying Liangxin Petrochemical Technology Development Limited Company’s parent company, will continue to practice the responsibilities and responsibilities of private enterprises and make positive contributions to social development.

The company is holding a video conference,Dongying Liangxin Petrochemical Technology Development Limited Company

The EMD Held a Quarterly Video Conference on Safety Management

The emergency management department held a quarterly Video Conference on centralized management of safety risks of hazardous chemicals

On July 29, the emergency management department held a quarterly video promotion meeting on the centralized management of safety risks of hazardous chemicals nationwide to report progress, analyze problems, exchange practices, strengthen measures, promote the implementation of key tasks, effectively prevent and control major safety risks, and create a stable safety environment for the success of the 20th CPC National Congress. Sunguangyu, member of the Party committee and vice minister of the emergency management department, attended the meeting and delivered a speech. Qichunxiao, the general manager of the group, and Qiao Huijie, the deputy general manager and director of safety and environmental protection, attended the video conference at the venue of the agricultural high-tech division in the Yellow River Delta.

However, from the mid-term evaluation results of centralized governance, there are still problems of uneven progress between regions, lagging progress of some special projects and low quality.

The meeting emphasized that we should have a clear understanding of the severe situation faced by the current safe production of hazardous chemicals and strengthen the sense of mission and urgency of doing a good job in centralized management. We should adhere to the problem orientation, anchor the goal of centralized governance, and make every effort to overcome difficulties. We should quickly wake up, be nervous, and take action. If there is a deviation in the direction of work, we should correct it in time. If the progress of work lags behind, we should pay close attention to make-up lessons, and accelerate the completion.

The meeting required that we should adhere to both the symptoms and root causes, accurately grasp the relationship between major risk prevention and control and centralized governance, promote major risk prevention and control and centralized governance as a whole, and prevent “two skins”. We should organically integrate centralized management and annual key work, integrate the requirements of centralized management tasks and measures into the major inspection of production safety and special safety actions, strengthen supervision and inspection and open and secret visits, do a good job in production safety in summer and flood seasons, strictly implement the main responsibility of enterprises, and resolutely prevent and contain major accidents and accidents with great impact.

At the meeting, Beijing, Liaoning, Zhejiang, Ningxia and other four provinces and CNPC made exchange speeches respectively, and the heads of relevant departments and bureaus, institutions and industry associations of the emergency management department and the main heads of relevant central enterprise safety management departments attended the meeting at the main venue; The heads of the emergency management departments at the provincial, municipal and county levels, as well as the relevant chemical parks and the main heads of enterprises attended the meeting at the branch venue.

Dongying Liangxin Petrochemical Technology Development Limited Company

The company is participating in the enterprise forum,Dongying Liangxin Petrochemical Technology Development Limited Company

The Group of Companies Participated in the Symposium on a Financial Project

The Junyuan Petroleum Group of Companies participated in the Symposium on project docking between financial leasing companies and small and medium-sized enterprises

On the morning of July 29, Dongying local financial supervision bureau held a symposium on the project docking between financial leasing companies and small and medium-sized enterprises. At the symposium, a number of financial leasing companies in Shandong Province were invited to carry out project face-to-face exchanges and interactions with small and medium-sized enterprises to carry out financing docking. Che Xiaojing, executive deputy general manager of the asset management company, attended the meeting and introduced the company’s projects.

The meeting pointed out that all financial leasing companies should take serving the real economy as the starting point and foothold, put forward reasonable financing plans and suggestions according to the financing needs of enterprises, help enterprises finance, and achieve steady development in the process of promoting local economic development. Small and medium-sized enterprises should further understand and be familiar with the financing method of financial leasing, effectively use financial leasing to alleviate capital problems, take the initiative to strengthen the connection with financial leasing companies, and invite financial leasing companies with promising cooperation to visit the enterprise on the spot to strive for cooperation.

Dongying Liangxin Petrochemical Technology Development Limited Company
Dongying Junyuan Petrochemical Technology Development Limited Company

Normal Pentane, Isopentane and Cyclopentane Blends

Pentane

We offer a large range of flammable and non-flammable blowing agents for Polyurethane (PU), Polystyrene (EPS, XPS) and Polyethelyne (PE) foams, which include liquids and blends.

Blowing Agent of Expendable Polystyrene, Polyurethane

BLENDS

With know how in formulating, handling and packaging blowing agents, we can also offer special blends such as :

n-Pentane/Isopentane
Cyclopentane/Isopentane
Cyclopentane/n-Pentane
Cyclopentane/Isopentane/n-Pentane

Blowing Agents/Pentane Blends

ISOPENTANE 70%, CYCLOPENTANE 30%
ISOPENANE 50%, CYCLOPENANE 50%
ISOPENTANE 30%, CYCLOPENTANE 70%
ISOPENANE 25%, CYCLOPENANE 75%
ISOPENTANE 20%, CYCLOPENTANE 80%
ISOPENANE 15%, CYCLOPENIANE 85%
ISOPENANE 10%, CYCLOPENANE 90%

Blowing Agents/Pentane Blends

ISOPENTANE 15%, NORMAL PENTANE 85%
ISOPENTANE 20%, NORMAL PENTANE 80%
ISOPENTANE 25%, NORMAL PENTANE 75%
ISOPENANE 30%, NORMAL PENANE 70%
ISOPENANE 40%, NORMALPENANE 60%
ISOPENANE 45%, NORMALPENANE 65%
ISOPENANE 50%, NORMALPENIANE 50%
ISOPENTANE 70%, NORMAL PENTANE 30%
ISOPENANE 75%, NORMAL PENANE 25%

PACKAGING

We offer a range of packaging from a bulk of 20 tonnes to a 1 litre sample.

BULK – up to 20 tonnes
CONTAINERS – 20″ GP container, 40″ GP container
DRUMS – 200 litres, 125KG, up to 150 KG
ISO Tanks – 14.5 MT, up to 17 MT
SAMPLE – 1 litre

Pentane Formula, Properties, Uses and Isomers

Pentane – Thermophysical Properties

Chemical, physical and thermal properties of pentane, also called n-pentane. Phase diagram included.

Physical Properties The boiling points of the pentane isomers range from about 9 to 36 °C. As is the case for other alkanes, the more branched isomers tend to have lower boiling points.

Usually, n-Pentane is used as a refrigeration or air conditioning substance, effectively replacing substances such as fluorinated hydrocarbons and ammonia. Here are some of its potential uses: refrigerant R601, non-polar solvent polyethylene process medium, how to use Isopentane? Isopentane is widely used. Firstly, it is an important refrigerant, which is used as the mixed refrigerant component of condensation inducer and LNG in LLDPE unit of olefin plant; Used for blending octane number of oil products;

Usage: isopentane is widely used. First, it is an important refrigerant of olefin unit, condensation inducer of LLDPE unit and LNG mixed refrigerant components; Used for blending oil octane number; It is widely used in organic synthesis reactions and the separation and purification of organic compounds; Secondly, isopentane dehydrogenation can be made of isoprene and isoprene, and isopentanol is obtained by chlorination and hydrolysis. It is also an important raw material for organic synthesis. Isopentane can also be used with n-pentane in EPS (expandable polystyrene) blowing agent, or with cyclopentane as rigid polyurethane blowing agent. It is mainly used in organic synthesis and also as a solvent.

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

Pentane, C5H12, is a clear colorless liquid with a petroleum-like odor. It belongs to the organic class alkanes, and is naturally present in crude oils and condensates. It is a component of some fuels and is employed as a specialty solvent in the laboratory.

The boling point 36°C/97°F, and the vapors are heavier than air. Both the liquid an the vapor are flammable.

The phase diagram of pentane is shown below the table.

Chemical, physical and thermal properties of pentane:
Values are given for liquid at 25oC /77oF / 298 K and 1 bara, if not other phase, temperature or pressure given.

Property Value Unit Value Unit Value Unit Value Unit
Autoignition temperature 533 K 260 °C 500 °F
Boiling Point 309.2 K 36.06 °C 96.9 °F
Critical density 3.22 mol/dm3 232 kg/m3 0.450 slug/ft3 14.5 lb/ft3
Critical pressure 3.36 MPa=MN/m2 33.6 bar 33.2 atm 487 psi=lbf/in2
Critical temperature 469.8 K 196.7 °C 386.0 °F
Critical volume 311 cm3/mol 0.00431 m3/kg 2.22 ft3/slug 0.0690 ft3/lb
Density 8606 mol/m3 620.9 kg/m3 1.205 slug/ft3 38.76 lb/ft3
Flammable, gas and liquid yes
Flash point 224 K -49 °C -56 °F
Gas constant, individual, R 115.2 J/kg K 0.03201 Wh/(kg K) 689.1 [ft lbf/slug °R] 21.42 [ft lbf/lb °R]
Gibbs free energy of formation (gas) -8 kJ/mol -111 kJ/kg -48 Btu/lb
Heat (enthalpy) of combustion (gas) -3535 kJ/mol -48996 kJ/kg -21.1 Btu/lb
Heat (enthalpy) of combustion (liquid) -3509 kJ/mol -48636 kJ/kg -20.9 Btu/lb
Heat (enthalpy) of formation (gas) -147.0 kJ/mol -2037 kJ/kg -876 Btu/lb
Heat (enthalpy) of formation (liquid) -173 kJ/mol -2398 kJ/kg -1031 Btu/lb
Heat (enthalpy) of fusion at -202 °F/-130°C 8.4 kJ/mol 116 kJ/kg 50.05 Btu/lb
Heat (enthalpy) of sublimation, at -202°F/-130°C 42 kJ/mol 582 kJ/kg 250 Btu/lb
Heat (enthalpy) of evaporation 26.4 kJ/mol 366 kJ/kg 157 Btu/lb
Heat capacity, Cp (gas) 120.0 J/mol K 1.66 kJ/kg K 0.397 Btu/lb°F or cal/g K
Specific heat, Cp (liquid) 168.0 J/mol K 2.33 kJ/kg K 0.556 Btu/lb°F or cal/g K
Specific heat, Cv (liquid) 125.0 J/mol K 1.73 kJ/kg K 0.414 Btu/lb°F or cal/g K
Ionization potential 10.34 eV
log KOW (Octanol/Water Partition Coefficient) 3.39
Melting point 143.48 K -129.7 °C -201.4 °F
Molecular Weight 72.149 g/mol 0.15906 lb/mol
Solubility in water, at 25°C 0.038 mg/ml
Sound velocity 1012 m/s 3319 ft/s 2267 mi/h
Specific Gravity (gas) (relativ to air) 2.48
Specific Gravity (liquid) (relativ to water) 0.63
Specific Heat Ratio (gas) – CP/CV 1.09
Specific Heat Ratio (liquid) – CP/CV 1.34
Specific Volume 0.0001162 m3/mol 0.0016106 m3/kg 0.8300514 ft3/slug 0.0257988 ft3/lb
Standard molar entropy, S° (gas) 348 J/mol K 4.82 kJ/kg K 1.15 Btu/lb °F
Standard molar entropy, S° (liquid) 263 J/mol K 3.65 kJ/kg K 0.87 Btu/lb °F
Surface tension 16.0 dynes/cm 0.016 N/m
Thermal Conductivity 0.111 W/m°C 0.064135 Btu/hr ft °F
Triple point pressure 7.63*10-8 MPa=MN/m2 7.63*10-7 bar 7.53*10-7 atm 1.11*10-5 psi=lbf/in2
Triple point temperature 143.5 K -129.7 °C -201.46 °F
Vapor (saturation) pressure 0.0685 MPa=MN/m2 514.0 mm Hg 0.6762 atm 9.94 psi=lbf/in2
Viscosity, dynamic (absolute) 0.2224 cP 149.4 [lbm /ft s*10-6] 4.64 [lbf s/ft2 *10-6]
Viscosity, kinematic 0.358 cSt 3.9 [ft2/s*10-6]

Density and specific weight of liquid pentane at varying temperature and atmospheric pressure, SI and Imperial units:

Density units conversion of Pentane:

kilogram/cubic meter [kg/m3] = gram/liter [g/l], kilogram/liter [kg/l] = gram/cubic centimeter [g/cm3]= ton(metric)/cubic meter [t/m3], once/gallon(US liquid) [oz/gal(US liq)] pound/cubic inch [lb/in3], pound/cubic foot [lb/ft3], pound/gallon(UK) [lb/gal(UK)], pound/gallon(US liquid) [lb/gal(US liq)], slug/cubic foot [sl/ft3], ton(short)/cubic yard [ton(short)/yd3], ton(long)/cubic yard [yd3]

  • 1 g/cm3 = 1 kg/l = 1000 kg/m3 = 62.428 lb/ft3 = 0.03613 lb/in3 = 1.9403 sl/ft3 = 10.0224 lb/gal(UK) = 8.3454 lb/gal(US liq) = 0.5780 oz/in= 0.7525 ton(long)/yr3
  • 1 g/l = 1 kg/m3 = 0.001 kg/l = 0.000001 kg/cm3 = 0.001 g/cm3 = 0.99885 oz/ft3  = 0.0005780 oz/in3 = 0.16036 oz/gal(UK) = 0.1335 oz/gal(US liq) = 0.06243 lb/ft3 = 3.6127×10-5 lb/in3 = 1.6856 lb/yd3 = 0.010022 lb/gal(UK) = 0.0083454 lb/gal(US liq) = 0.0007525 ton(long)/yd= 0.0008428 ton(short)/yd3
  • 1 kg/l = 1 g/cm3 = 1000 kg/m3 = 62.428 lb/ft3 = 0.03613 lb/in3 = 1.9403 sl/ft3 = 8.3454 lb/gal(US liq) = 0.5780 oz/in= 0.7525 ton(long)/yr3
  • 1 kg/m3 = 1 g/l = 0.001 kg/l = 0.000001 kg/cm3 = 0.001 g/cm3 = 0.99885 oz/ft3  = 0.0005780 oz/in3 = 0.16036 oz/gal(UK) = 0.1335 oz/gal(US liq) = 0.06243 lb/ft3 = 3.6127×10-5 lb/in3 = 1.6856 lb/yd3 = 0.010022 lb/gal(UK) = 0.008345 lb/gal(US liq) = 0.0007525 ton(long)/yd = 0.0008428 ton(short)/yd
  • 1 lb/ft3 = 27 lb/yd3 = 0.009259 oz/in= 0.0005787 lb/in= 16.01845 kg/m3 = 0.01602 g/cm3  = 0.1605 lb/gal(UK) = 0.1349 lb/gal(US liq) = 2.5687 oz/gal(UK) = 2.1389 oz/gal(US liq) = 0.01205 ton(long)/yd3 = 0.0135 ton(short)/yd3
  • 1 lb/gal(UK) = 0.8327 lb/gal(US liq) = 16 oz/gal(UK) = 13.323 oz/gal(US liq) = 168.179 lb/yd3 = 6.2288 lb/ft3 = 0.003605 lb/in3 = 0.05767 oz/in = 99.7764 kg/m3 = 0.09977 g/cm3  = 0.07508 ton(long)/yd3 = 0.08409 ton(short)/yd3
  • 1 lb/gal(US liq) = 1.2009 lb/gal(UK) = 19.215 oz/gal(UK) = 16 oz/gal(US liq) = 201.97 lb/yd3 = 7.4805 lb/ft3 = 0.004329 lb/in3 = 0.06926 oz/in = 119.826 kg/m3 = 0.1198 g/cm3  = 0.09017 ton(long)/yd3 = 0.1010 ton(short)/yd3
  • 1 lb/in3 = 1728 lb/ft3 = 46656 lb/yd3 = 16 oz/in= 27680 kg/m3 = 27.680 g/cm3  = 277.419 lb/gal(UK) = 231 lb/gal(US liq) =4438.7 oz/gal(UK) = 3696 oz/gal(US liq) = 20.8286 ton(long)/yd3 = 23.3280 ton(short)/yd3
  • 1 oz/gal(UK) =  0.8327 oz/gal(US liq) = 6.2360 kg/m3 = 6.2288 oz/ft3 = 0.3893 lb/ft3 = 10.5112 lb/yd3
  • 1 oz/gal(US liq) = 1.2009 oz/gal(UK) = 7.4892 kg/m3 = 7.4805 oz/ft3 = 0.4675 lb/ft3 = 12.6234 lb/yd3
  • 1 sl/ft3 = 515.3788 kg/m3 = 514.7848 oz/ft3 = 0.2979 oz/in3 = 32.1741 lb/ft3 = 82.645 oz/gal(UK) = 68.817 oz/gal(US liq) 
  • 1 ton(long)/yd3 = 1.12 ton(short)/yd3 = 1328.94 kg/m3 = 0.7682 oz/in3 = 82.963 lb/ft3 = 2240 lb/yd3 = 2.5786 sl/ft3 = 13.319 lb/gal(UK) = 11.0905 lb/gal(US liq)
  • 1 ton(short)/yd3 = 0.8929 ton(long)/yd3 = 1186.55 kg/m3 = 0.6859 oz/in3 = 74.074 lb/ft3 = 2000 lb/yd3 = 2.3023 sl/ft3 = 11.8921 lb/gal(UK) = 9.9023 lb/gal(US liq)


Pentane Phase Digaram

HR director is interviewing, Dongying Liangxin Petrochemical Technology Development Limited Company

Graduate Students from OUC Come to Our Company for Exchange

Graduate students from Ocean University of China come to our company for exchange and visit

On the morning of July 22, a group of 5 graduate students majoring in Applied Chemistry from Ocean University of China came to our company for exchange and visit. Sun peisheng, the assistant general manager of the company, Wei fuchang, the director of the production and operation center, and chen huimin, the manager of the general office, attended the exchange.

Chen Huimin extended a warm welcome to the exchange students of Ocean University of China and introduced the company in detail. The graduate students listened carefully to the introduction and watched the company’s promotional videos. Wei fuchang led the exchange students to visit the factory and gave relevant explanations. Sun Peisheng had in-depth exchanges with students in the company’s products, research directions, cooperation fields and other aspects. This activity created opportunities for communication and learning between the company and the school, and laid a good foundation for the next step of school and enterprise cooperation.

Dongying Liangxin Petrochemical Technology Development Limited Company

The director of human resources department is talking with the presidents of major universities, Dongying Liangxin Petrochemical Technology Development Limited Company

DVCST Visited Our Company for Exchange and Investigation

Dongying Vocational College of Science and Technology visited our Company for Exchange and Investigation

On the morning of July 13, Miao Jin, Dean of the school of Economics and Management of Dongying Vocational College of Science and Technology, and his delegation came to our company for exchange and investigation. Chen Huimin, Manager of the General Office of the company, participated in this exchange activity. Chen Huimin extended a warm welcome to the leaders of the college, and the two sides had an in-depth exchange and Discussion on how to deepen school and enterprise cooperation. Miao Jin expressed the hope to reach long-term practical training friendly cooperation with the company.

Through this exchange activity, the communication and understanding between the company and the school have been strengthened, the friendly relationship between the two sides has been enhanced, and the foundation has been laid for further cooperation.

Dongying Liangxin Petrochemical Technology Development Limited Company, a subsidiary of Junyuan Petroleum Group, has been engaged in the export of butane, pentane, hexane and heptane since 2006. More than 15 years of experience enables you to rest without worrying about goods transportation.

Major customers include PetroChina, Sinopec, Shell, BASF, Saudi Basic Industries Corporation, China Coal, geothermal power plants and other foaming plants.
SGS, CIQ, BV, Rosh, ISO certificates are available.
Production Capacity: 1000,000 tons / year
After Sales Service: Dongying Liangxin Petrochemical Technology Development Limited Company enjoys a good reputation in the alkane industry. You can trust us completely.
Quality Assurance
As a quality-oriented company, we spare no effort to provide customers with the best range of products. In addition, we have hired a team of quality analysts to ensure that our industrial chemicals series meet international standards. Our quality analyst team maintains strict monitoring of the handling of chemicals and ensures that the range of various parameters is checked before sending chemicals to the client. The various parameters of our csindustrial chemical series tests are as follows:
Pure
PH value
Precise composition
For more information: info@junyuanpetroleumgroup.com

n-Pentane Manufacturer

Industrial application of Pentane as a new welding and cutting fuel in China for the first time

The press conference on industrial application results of pentane as a new welding and cutting fuel was held at China Shipbuilding Group Guangzhou shipbuilding International Co., Ltd. This achievement is the first successful industrial application of pentane as a new welding and cutting fuel in China.

Pentane” usually refers to n-pentane, with the chemical formula of C5H12, which is the fifth member of alkanes. Pentane can be obtained from catalytic cracking and thermal decomposition of natural gas or petroleum, so pentane is also a by-product of oil refining process. In the past, it was mainly used to make low melting point organic solventsfoaming agents for plastic industry, artificial ice, etc. At the same time, pentane also has the characteristics of high combustion calorific value. After full combustion, pentane is safer and more environmentally friendly than conventional natural gas and other welding and cutting fuels. It is an ideal substitute for conventional fuels. Its high calorific value can also perfectly solve the problem of cutting thick ship plates and special steel plates in the shipbuilding industry.

It is understood that in order to promote the transformation and upgrading of product structure, Guangzhou shipbuilding international has undertaken the largest order for super large container ships with more than 16,000 containers in South China. The crack arrest steel applied to the deck, hatch enclosure and other key parts of the super large container ship has large thickness and high strength. It can achieve one-time forming by cutting with pentane with higher fuel value.

In three years, Guangzhou shipbuilding international and Shenghuo energy technology (Guangdong) Co., Ltd. have jointly developed a mobile blended light oil gasification system, which has solved the technical problems of stable gasification technology of liquid pentane welding and cutting fluid under normal temperature and pressure, pipeline transportation and pressure allocation of gasification equipment, and realized that pentane welding and cutting fluid can be supplied in the form of tank, and pentane welding and cutting fluid supply points can also be established through the gasification system, It provides a new green fuel choice for the industrial application of shipbuilding enterprises.

After application and inspection by a third-party testing agency, pentane welding and cutting fluid has obvious fuel saving effect, and the consumption of fuel and oxygen has been reduced by more than 30%; Cutting efficiency is close to or slightly higher than that of the existing natural gas; Compared with natural gas, it has obvious advantages in reducing slag hanging and preventing edge melting in medium and thick ship plate cutting.

A device for flame cutting and welding with pentane liquid as fuel comprises a jet suction cutting and welding torch, an evaporator and an oxygen cylinder. The oxygen joint of the jet suction cutting and welding torch is connected with a pressure regulating valve installed on the oxygen cylinder through a hose, and the gas joint of the jet suction cutting and welding torch is connected with the evaporator through a hose. The gas joint is equipped with a gas valve, and the evaporator is also equipped with a gas valve. The evaporator is equipped with an explosion-proof wire and a sieve plate, The screen plate is located at the bottom of the explosion-proof wire, and the lower part of the screen plate is equipped with a check valve and a silencing distributor. One end of the check valve is connected with the silencing distributor, and the other end is connected with the breathing valve located outside the evaporator through a pipe. A floating ball valve is also installed inside the evaporator, which is connected with the make-up valve outside the evaporator through a pipeline. After adopting the above device, compared with the gasoline cutting welder, the ignition performance is better and the stability is higher. The flame temperature of cutting and welding is up to 260 (RC ~ 280 (TC), and it is easy to adjust to carbonization flame, neutral flame and oxidation flame. When acetylene is burning, the carbonization flame has thick black smoke. The utility model does not have any black smoke, so the combustion ignition is easy, the flame is stable, and there is no backfire. The operation is simple. When cutting and welding is stopped, there is no smoke in the evaporator

It can stop working automatically because of negative pressure. The evaporator of the utility model has the advantages of simple structure, easy fabrication and low cost. Due to the negative pressure working condition, and an appropriate amount of explosion-proof wire is filled in the evaporator, the safety is very high. Practice has proved that the energy saving of the scheme of the utility model is more than 50% compared with that of acetylene gas and more than 25% compared with that of propane gas. Since the combustion temperature is about 400-500 ℃ higher than that of propane gas, steel plates or components with a thickness of less than 300mm can be cut smoothly. The steel plates cut by the combustion temperature are easier to process than the cutting edges cut by acetylene, and there is no slag at the bottom of the cutting edges, which is suitable for industrial needs. Figure 1 is the structural diagram of the device of the utility model. Specific implementation mode: the utility model is further described below in combination with the attached drawings. As shown in Figure L, this embodiment includes a jet suction cutting and welding torch L, an evaporator 2 and an oxygen cylinder 3. The oxygen joint of the jet suction cutting and welding torch 1 is connected with the pressure regulating valve 11 installed on the oxygen cylinder 3 through a hose. The gas joint of the jet suction cutting and welding torch 1 is connected with the evaporator 2 through a hose. The gas joint is equipped with a gas valve 12, and the evaporator 2 is also equipped with a gas valve 4. The evaporator is equipped with an explosion-proof wire 7 and a sieve plate 8, The screen plate 8 is located at the bottom of the explosion-proof wire 7. The lower part of the screen plate 8 is equipped with a check valve 9 and a silencing distributor 10. One end of the check valve 9 is connected with the silencing distributor 10, and the other end is connected with the breather valve 5 located outside the evaporator 2 through a pipe. A floating ball valve 13 is also installed inside the evaporator 2, and the floating ball valve 13 is connected with the make-up valve 6 outside the evaporator through a pipe. The specific working method of the utility model is as follows: when the regulating valve 11 on the oxygen cylinder 3 is opened and adjusted to the required pressure, the preheating valve 14 in the jet type cutting and welding torch L is opened, the jet suction device in the jet type cutting and welding torch 1 will generate negative pressure in the fuel channel, and then the gas valve 12 on the gas joint and the evaporator gas valve 4 are opened. The negative pressure will directly generate negative pressure in the evaporator 2 through the connecting pipe, and the breathing valve 5 is opened, The air flows upward through the breather valve 5, the check valve 9 and the silencing distributor 10, is evenly distributed through the sieve plate 8, and is violently mixed with the liquid amyl in the boiling state in the explosion-proof wire 7. The check valve 9 in the evaporator 2 is used to prevent the internal liquid from leaking out when the evaporator 2 is operating accidentally. Due to the low latent heat of vaporization and low boiling point of pentane, it can quickly absorb the heat of the external environment of the evaporator 2 made of metal and evaporate into a mixture of pentane gas and air with high concentration under the action of negative pressure. Under the action of negative pressure, pentane is continuously pumped into its injection and suction device by the injection and suction torch 1 and mixed with oxygen in proportion to form a fuel gas which is injected into the nozzle for combustion to achieve the purpose of cutting and welding. The pentane liquid can be filled by opening the make-up valve 6, which is sucked from the fuel storage tank to the evaporator 2. When the liquid level reaches a certain height, it will be automatically closed by the float valve 13. If ioo cutting torch is adopted for the above-mentioned jet suction cutting torch, the oxygen pressure of the cutting torch is 0.6MPa, the negative pressure of the gas interface is about 0.04 ~ 0.05Mpa, and the evaporation capacity of pentane liquid is 0.26 ~ 0.3l/h. The flame of the cutting torch can be easily adjusted to neutral flame, and the flame temperature is 2600 ° C ~ 2800 ° C, which can smoothly cut 100mm thick steel plate; If No. 8 jet suction welding torch is used for jet suction cutting torch 1, the required oxygen pressure is 03mpa, the negative pressure of gas interface is 0.035 ~ 0.04MPa, and the evaporation capacity of pentane liquid is 0.1 ~ 0.12l/h. The flame of the cutting torch can be easily adjusted to oxidation flame, neutral flame and carbonization flame, The flame temperature is 2600’c ~ 280 (TC, welding can be carried out smoothly. To sum up, the advantages of the utility model are: 1. The ignition performance of the utility model is better than that of the gasoline cutting welder, and the stability is high. The original propane injection cutting torch and welding torch do not need to be matched with the specially manufactured cutting torch or welding torch, which can save the enterprise’s equipment reinvestment investment and facilitate the purchase of vulnerable parts; 2. The safety is high, even if the cutting torch or welding torch is broken or accidentally damaged when working, it will not produce Danger caused by leakage of raw gas. Since the evaporator is filled with explosion-proof wire according to the standard, no explosion will occur; 3. The energy-saving effect is remarkable, and the production cost is greatly reduced; 5. As a by-product of petroleum industry and a class B green fuel, the waste gas after combustion is harmless to human body, which not only solves the problem of by-product of petroleum industry, but also ensures the safety and health of users; 6. The efficiency of cutting and welding has been improved. The cutting speed is slightly faster than that of acetylene. It is easy to operate and master. It is convenient to carry out construction outside. The utility model can not only be applied to the cutting of steel and the welding of metal, but also can be widely applied to glass fusion to replace the commonly used propane gas and natural gas, and has remarkable safety and energy-saving effects.

1. The device for flame cutting and welding with pentane liquid as fuel includes a jet suction cutting and welding torch (1), an evaporator (2) and an oxygen cylinder (3), which is characterized in that the oxygen joint of the jet suction cutting and welding torch (1) is connected with the pressure regulating valve (11) installed on the oxygen cylinder (3) through a hose, and the gas joint of the jet suction cutting and welding torch (1) is connected with the evaporator (2) through a hose, wherein the gas joint is provided with a gas valve (12), and the evaporator (2) is also provided with a gas valve (4), An explosion-proof wire (7) and a sieve plate (8) are installed inside the evaporator, the sieve plate (8) is located at the bottom of the explosion-proof wire (7), a check valve (9) and a silencing distributor (10) are installed below the sieve plate (8), one end of the check valve (9) is connected with the silencing distributor (10), and the other end is connected with the breather valve (5) located outside the evaporator (2) through a pipe.

Pentanes

PRODUCT DESCRIPTIONPurity Percent
n-Pentane99%, 95% 
Isopentane  99%, 96%
n- Pentane / Isopentane Blend20-80%, 30-70%
Pentane Products List
n-Pentane and applications

n-Pentane, 99%, n-Pentane, 95%
CAS NO 109-66-0
Applications: Blowing Agents, Plastics Industry, Geothermal Energy, Personal Care Products, Gasoline

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