Archives October 2020

[Today’s Crude Oil]: European and American countries strictly control the epidemic once again, and international oil prices fall back

[today’s crude oil]: European and American countries strictly control the epidemic once again, and international oil prices fall back
European countries once again strictly control the epidemic and re restrict travel may reduce the demand for oil and the international oil price will fall back. However, U.S. crude oil inventories fell, and international oil prices were off their intraday lows. On Thursday (October 15), the settlement price of West Texas light oil in November 2020 on the New York Mercantile futures exchange was $40.96, down $0.08, or 0.2%, from the previous trading day, with a trading range of 39.22-41.29; the settlement price of December 2020 futures of Brent crude oil in London intercontinental exchange was $43.16 per barrel, down $0.16, or 0.4%, from the previous trading day, with a trading range of 42.13-43 45 dollars.
Some European countries are resuming curfews and closures in response to a surge in the number of new crown cases, and Britain announced that stricter restrictions would be imposed in London on Friday. French President Marcon has announced curfews in nine French cities, including Paris, to curb the spread of the new crown. New coronal infections have surged in the United States, and states have tightened social restrictions. Unemployment continued to rise in the United States, which also brought a negative atmosphere to the oil market. The number of jobless benefits rose to a seven week high of 898000 in the week ending October 10, up 53000 from the previous week, according to data from the U.S. Department of labor on October 15. Vitol, Trafigura and Cornwall, the world’s largest oil traders, all said the recovery in oil demand would be slow due to the rebound in the outbreak.
Robert yawger, head of Mizuho energy futures, said the U.S. Energy Information Administration’s inventory report put a hold on the decline in oil prices, otherwise a crash could occur earlier on Thursday.
Gasoline demand in the United States decreased while distillate demand increased. According to the data of the energy information administration of the United States, as of October 9, 2020, the total demand for refined oil in the United States averaged 18.427 million barrels per day, 12.6% lower than that in the same period last year; the average daily demand for motor gasoline was 8.629 million barrels, 7.5% lower than that of the same period last year; and the average demand for distillate oil was 3.914 million barrels per day, It was 3.7% lower than the same period last year, and the daily average demand of kerosene aviation fuel was 41.8% lower than that of the same period last year. In a single week’s demand, the average daily oil demand in the United States was 19.475 million barrels, 1.13 million barrels higher than that of the previous week; the daily demand of gasoline in the United States was 8.576 million barrels, which was 320000 barrels lower than that of the previous week; the average daily demand of distillate oil was 4.175 million barrels, 307000 barrels higher than the average of the previous week.
Hurricane Delta has led to a sharp drop in oil and gas production in the Gulf region of the United States, a decrease in crude oil imports, and a decline in U.S. crude oil inventories, as well as a decrease in U.S. gasoline and distillate stocks over the same period. U.S. crude oil inventory was 48910.9 million barrels in the week ending October 9, down 3.82 million barrels from the previous week; total U.S. gasoline inventory was 225.21 million barrels, down 1.63 million barrels from the previous week; and distillate oil inventory was 164.55.1 million barrels, down 7.24 million barrels from the previous week. Crude oil inventory was 12.5% higher than that of the same period last year, 11% higher than that of the same period of the past five years, gasoline inventory was 0.5% lower than that of the same period of last year, 1% lower than that of the same period of the past five years, and the stock of distillate oil was 33.2% higher than that of the same period of last five years and 19% higher than that of the same period of the past five years. Total commercial oil inventories in the United States fell by 16.8 million barrels. The average processing volume of American refineries was 13.577 million barrels per day, 277000 barrels less than the previous week; the operating rate of refineries was 75.1%, 2.0 percentage points lower than that of the previous week. Last week, US crude oil imports averaged 5.286 million barrels a day, a decrease of 447000 barrels compared with the previous week. The average daily import of refined oil was 203.6 barrels, down 121000 barrels from the previous week. In the past week, US strategic oil reserves fell by 1.16 million barrels to 64084.7 million barrels.
The decline of U.S. crude oil inventory was concentrated in the Gulf of Mexico region. As of October 9, crude oil inventory in the Gulf region of the United States was 256.33 million barrels, down 5.12 million barrels from the previous week; the highly concerned crude oil inventory in Cushing, Oklahoma, was 59.442 million barrels, an increase of 2.906 million barrels.
US crude oil exports fell to the lowest level in 14 months. According to the data, for the week ending October 2, the average daily crude oil export volume of the United States was 2135000 barrels, 524000 barrels less than that of the previous week, and 1113000 barrels lower than that of the same period last year. In the past four weeks, the average daily export volume of US crude oil was 2.832 million barrels, down 9.4% from the same period last year. Since the beginning of this year, the average daily export of US crude oil is 3.132 million barrels, an increase of 8.4% over the same period last year. In the past week, US crude oil net imports averaged 3.151 million barrels a day, an increase of 77000 barrels over the previous week. The total net oil exports of the United States averaged 3.354 million barrels a day, an increase of 271000 barrels over the previous week. The total net imports of crude oil and refined oil in the United States averaged 204000 barrels a day, an increase of 193000 barrels over the previous week.
For the week ending October 9, the average daily output of US crude oil was 10.5 million barrels, a decrease of 500000 barrels compared with the average output of the previous Sunday and a decrease of 2.1 million barrels over the same period of last year; for the four weeks ending October 10, the average daily output of US crude oil was 10.725 million barrels, 14.4% lower than that of the same period last year.
According to the U.S. safety and environmental enforcement agency, as of noon on October 15, about 24% of the offshore oil and gas fields in the U.S. Gulf region had lost production by 440000 barrels a day. S & P’s analysts estimate that it may take nearly two weeks for the region to fully resume production.

Annual output of 1 million tons of polystyrene project settled in Zhoushan,China

Exclusive news: annual output of 1 million tons of polystyrene project settled in Zhoushan
The Management Committee of marine industry cluster zone of Zhoushan archipelago new area of Zhejiang Province and Zhejiang Yisu New Material Technology Co., Ltd. signed a project investment agreement. The new material project with a total investment of 2 billion yuan and an estimated annual output value of 10 billion yuan was officially settled in Zhoushan. The new material project with an annual output of 1 million tons of polystyrene, with a total investment of 2 billion yuan, is expected to use 130000 square meters of land. The project will be constructed in two phases. The first phase is planned to start construction next month, and is expected to start trial production in August next year, with an annual output of 400000 tons of polystyrene; the second phase is planned to start construction in October next year and complete in October 2022. The annual sales volume of the two phases can reach 10 billion yuan.

CHINESE YUAN RENMINBI EXCHANGE RATES TABLE

Top 10Oct 18, 2020 00:50 UTC

Chinese Yuan Renminbi1.00 CNYinv. 1.00 CNY
US Dollar0.1493226.696943
Euro0.1274447.846600
British Pound0.1156198.649083
Indian Rupee10.9683380.091172
Australian Dollar0.2109064.741455
Canadian Dollar0.1969435.077606
Singapore Dollar0.2029154.928164
Swiss Franc0.1365917.321101
Malaysian Ringgit0.6194001.614467
Japanese Yen15.7383420.063539

Percent Change in the Last 24 Hours

  • EUR/USD-0.01051%
  • USD/JPY-0.00174%
  • GBP/USD+0.00314%
  • USD/CHF+0.00236%
  • USD/CAD-0.01163%
  • EUR/JPY-0.01225%
  • AUD/USD+0.01374%
  • CNY/USD+0.00947%

Expandable Polystyrene Beads The foam pattern is formed from expandable beads (commonly polystyrene) which contain pentane (5-7 wt%) as a blowing/expansion agent. The raw EPS beads (EPS= expandable polystyrene) are delivered at a density of about 38 #/cubic foot in a wide range of initial sizes (10 to 80 mils diameter)

Expandable Polystyrene / EPS: This is PS Foam that uses Pentane gas (C5H12) as the blowing agent. During the material production process called “Polymerisation” the polystyrene resin granules impregnated with the blowing agent. EPS production processes begin in the pre-expansion process where the EPS bead will expand by the heat of steam.

n-Pentane, CAS:109-66-0
Isopentane, CAS:78-78-4
Pentane Blends, CAS:109-66-0
n-Hexane, CAS:110-54-3
Isohexane, CAS:107-83-5
n-Heptane, CAS:142-82-5

  • n-Pentane
  • CAS Number: 109-66-0
  • MF: C5H12
  • MW: 72.149
  • Catalog:Alkane
  • Density: 0.6±0.1 g/cm3
  • Boiling Point: 35.2±3.0 °C at 760 mmHg
  • Melting Point: -130ºC
  • Flash Point: -49.4±0.0 °C

Isohexane – CAS 107-83-5

Chemical NameProduct NameCAS No.
IsohexaneIsohexane101316-67-0(107-83-5)
Hexane (mixture of isomers) ≥99% ACS
Danger

Synonyms: 1,1-Dimethylbutane , Isohexane

Formula: C₆H₁₄
MW: 86.18 g/mol
Boiling Pt: 60 °C (760 mmHg)
Melting Pt: –154 °C
Density: 0.653 g/cm³ (20 °C)
Flash Pt: –23 °C
Storage Temperature: Ambient
MDL Number: MFCD00009406
CAS Number: 107-83-5
EINECS: 203-523-4
UN: 1208
ADR: 3,II

Specification Test Results

AppearanceClear colorless Liquid
Infrared spectrumConforms
Refractive index1.3700 to 1.3720 (20°C, 589 nm)
GC≥99.0 %

Synonyms: Hexanes , Isohexane

Meets ACS specifications for general use.

Formula: H₃C(CH₂)₄CH₃
MW: 86.18 g/mol
Boiling Pt: 68…70 °C (1013 hPa)
Melting Pt: –95 °C
Density: 0.66 g/cm³ (20 °C)
Flash Pt: –22 °C
Storage Temperature: Ambient
MDL Number: MFCD02179311
CAS Number: 110-54-3
EINECS: 203-777-6
UN: 1208
ADR: 3,II
Manufacturer: Junyuan Petroleum Group

Specification Test Results

AppearanceClear
Water (K.F.)Less than 0.010%
ResidueLess than 0.001% (0.0010 g/145 mL)
GC PurityGreater than 98.5% n-hexane (n-C6) and C6 isomers (Typical – 99.9+%)
n-HexaneGreater than 60.0%
Color (APHA)Less than 10
Water-soluble titrable acidLess than 0.3 meq/g (Not more than 1.0 mL of
Sulfur compounds (as S)Less than 0.005% (Absence of precipitate)
ThiophenePasses test (Acid layer should not be blue or green)

Product Description

Catalogue NumberJPG171727
Chemical Name2-Methylpentane
Synonyms1,1-Dimethylbutane; Isohexane; Kyowasol C 600M; Kyowazol C 600; NSC 66496
CAS Number107-83-5
Molecular FormulaC₆H₁₄
AppearanceColourless Oil
Molecular Weight86.18
Storage4°C
SolubilityChloroform (Soluble), Ethyl Acetate (Slightly)
StabilityVolatile
CategoryBuilding Blocks; Miscellaneous;
Applications2-Methylpentane is used as a raw material/intermediate in organic synthesis, rubber solvent, and vegetable oil extraction solvent.
ReferencesChoi, D., et al.: Adv. Funct. Mater. 25, 920 (2015)

DESCRIPTION

General description

2-Methylpentane is a type of branched alkane classified under the volatile organic compounds (VOCs) family of chemicals.

Application

Refer to the product′s Certificate of Analysis for more information on a suitable instrument technique. Contact Technical Service for further support.2-Methylpentane has been used as a reference standard for the determination of 2-methylpentane as odor marker of lung cancer in human breath samples by gas chromatography-time of flight mass spectrometry (GC-TOF MS). It may be used as a reference standard for the determination of 2-methylpentane in virgin olive oil samples by headspace solid-phase microextraction (SPME) followed by analysis using GC-MS coupled to flame ionization detector (FID), in different microenvironments by multibed adsorption and short-path thermal desorption followed by GC-MS and in exhaled air of patients with non-small cells lung cancer (NSCLC) by GC-MS.

Global Specialty Solvents Distribution

Junyuan Petroleum Group offers a wide variety of general applications solvents of the following to meet our customers’ needs. Our specialty solvents have a guaranteed purity of greater than or equal to 99.9% for applications that require higher purities such as specialty organic synthesis. Junyuan Petroleum Group is a leading provider in the world of spcialty solvents. We cover wide range of specifications – from industrial grade to highest purity. We cover 90 percent of China markets across more than 30 industries through our network of strategic industry partners that spans the nation.

Product NameCAS NUMBERDescriptions
Normal Pentane106-66-0hydrocarbon of the methane series, existing in three liquid isomeric forms. Also called normal pentane. the most important isomer of pentane, a colorless, flammable, water-insoluble, very volatile liquid, C5H12, obtained from petroleum by distillation: used chiefly as a solvent and in medicine as an anesthetic.
Normal Hexnae110-54-3Hexane is a straight-chain alkane with six carbon atoms and has the molecular formula C₆H₁₄. Hexane is a significant constituent of gasoline. It is a colorless liquid, odorless when pure, and with boiling points approximately 69 °C. It is widely used as a cheap, relatively safe, largely unreactive, and easily evaporated non-polar solvent.
Isopentae78-78-4Isopentane
Isopentane, also called methylbutane or 2-methylbutane, is a branched-chain saturated hydrocarbon with five carbon atoms, with formula C₅H₁₂ or CH(CH₃). Isopentane is an extremely volatile and extremely flammable liquid at room temperature and pressure. It is also the least dense liquid at standard conditions. The normal boiling point is just a few degrees above room temperature and isopentane will readily boil and evaporate away on a warm day.
Boiling point: 81.86°F (27.70°C)
Density: 0.62 g/cm³
Chemical formula: C5H12
Average Molar mass: 72.15 g/mol
Classification: Alkane
Isohexnae107-83-52-Methylpentane
Branched-Chain Alkane
2-Methylpentane, trivially known as isohexane, is a branched-chain alkane with the molecular formula C₆H₁₄. It is a structural isomer of hexane composed of a methyl group bonded to the second carbon atom in a pentane chain.
Boiling point: 140°F (60°C)
Chemical formula: C6H14
Melting point: -243.40°F (-153°C)
Average Molar mass: 86.18 g/mol
Normal Heptane142-82-5Image result for Normal HeptaneImage result for Normal HeptaneImage result for Normal HeptaneImage result for Normal HeptaneImage result for Normal Heptane
See all images
Heptane
Straight-Chain Alkane
Heptane or n-heptane is the straight-chain alkane with the chemical formula H₃C(CH₂)₅CH₃ or C₇H₁₆, and is one of the main components of gasoline. When used as a test fuel component in anti-knock test engines, a 100% heptane fuel is the zero point of the octane rating scale. Octane number equates to the anti-knock qualities of a comparison mixture of heptane and isooctane which is expressed as the percentage of isooctane in heptane and is listed on pumps for gasoline dispensed globally.
Density: 0.68 g/cm³
Boiling point: 209.16°F (98.42°C)
Chemical formula: C7H16
Average Molar mass: 100.21 g/mol
D 20 solvent64742-94-5D-20 is a powerful medium to quick break solvent degreaser specifically designed to deal with stubborn deposits of grease, oil and dirt. Unlike other solvent degreasers D-20 has been designed with the safety of the user as a priority. D-20 is non-flammable, non-hazardous and the rate at which D-20 turns to vapour is lower than competitor products.
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With 11 years of pioneering innovative specialty solvents, the brand of Junyuan Petroleum Group has become the global quality standard for the industry and a trusted partner for businesses across industries in more than 56 countries.

n-Heptane,99%, CAS 142-82-5

Project AnalysisQuality Controlling IndexTest Results
Content of n-Heptane, w%≥9999.96
Distillation range, primary distillation point, dry point (℃)≥94 ≤9995-98
Density (20 ℃), kg / m3650-690683
Bromine index, MGBR / 100g≤1000.04
Saybolt Colour≥+28+30
Sulfur content, mg/kg≤20.25
Micro aromatic hydrocarbon, ppm≤10Not Found
    Water w/v%≤0.10.0058
Nonvolatile content, w/v%≤0.0050.0002

n-Heptane

May 1994
Immediately Dangerous to Life or Health Concentrations (IDLH)

CAS number: 142–82–5

NIOSH REL: 85 ppm (350 mg/m3) TWA,

440 ppm (1,800 mg/m3) 15-minute CEILING

Current OSHA PEL: 500 ppm (2,000 mg/m3) TWA

1989 OSHA PEL 400 ppm (1600 mg/m3) TWA, 500 ppm (2,000 mg/m3) STEL

1993-1994 ACGIH TLV: 400 ppm (1,640 mg/m3) TWA, 500 ppm (2,050 mg/m3) STEL

Description of Substance: Colorless liquid with a gasoline-like odor.

LEL:. . 1.05% (10% LEL, 1,050 ppm)

Original (SCP) IDLH: 5,000 ppm

Basis for original (SCP) IDLH: The chosen IDLH is based on the statement by Patty [1963] that a 15-minute exposure to 5,000 ppm produced a state of intoxication characterized by uncontrolled hilarity in some individuals and in others a stupor lasting for 30 minutes after the exposure [Patty and Yant 1929]. According to Patty [1963], a 4-minute exposure to this same concentration produces vertigo and incoordination [Patty and Yant 1929]. These symptoms described by Patty [1963] could perhaps impede escape.

Short-term exposure guidelines: None developed

ACUTE TOXICITY DATA

Lethal concentration data:


Species

Reference
LC50(ppm)LCLo(ppm)
Time
Adjusted 0.5-hrLC (CF)Derivedvalue
HumanMouseMouseFlury and Zernik 1931Marhold 1986Swann et al. 1974—–17,986—–16,000—–15,000?2 hr30 min?28,778 ppm (1.6)15,000 ppm (1.0)?2,878 ppm1,500 ppm

Other human data: Inhalation of 1,000 ppm for 6 minutes was associated with slight dizziness [Patty and Yant 1929]. Exposure to 5,000 ppm for 4 minutes produced complaints of nausea, a loss of appetite, vertigo, and incoordination [Patty and Yant 1929]. A 15-minute exposure to 5,000 ppm produced a state of intoxication characterized by uncontrolled hilarity in some individuals and in others a stupor lasting for 30 minutes after the exposure [Patty and Yant 1929].

Revised IDLH: 750 ppmBasis for revised IDLH: The revised IDLH for n-heptane is 750 ppm based on acute inhalation toxicity data in humans [Patty and Yant 1929].

REFERENCES:

1. Flury F, Zernik F [1931]. Schädliche gase dämpfe, nebel, rauch- und staubarten. Berlin, Germany: Verlag von Julius Springer, pp. 257-264 (in German).

2. Marhold J [1986]. Prehled Prumyslove Toxikologie, Organicke Latky. Prague, Czechoslovakia: Avicenum, p. 9 (in Czechoslovakian).

3. Patty FA, ed. [1963]. Industrial hygiene and toxicology. 2nd rev. ed. Vol. II. Toxicology. New York, NY: Interscience Publishers, Inc., pp. 1198-1199.

4. Patty FA, Yant WP [1929]. Odor intensity and symptoms produced by commercial propane, butane, pentane, hexane, and heptane vapor. Pittsburgh, PA: Department of Commerce, U.S. Bureau of Mines, Report of Investigations, No. 2979, pp. 1-10.

5. Swann HE Jr, Kwon BK, Hogan GK, Snellings WM [1974]. Acute inhalation toxicity of volatile hydrocarbons. Am Ind Hyg Assoc J 35:511-518.

Junyuan Heptane is commercially available as mixed isomers for use in paints and coatings, as the rubber cement solvent “Bestine”, the outdoor stove fuel “Powerfuel” by Primus, as pure n -heptane for research and development and pharmaceutical manufacturing and as a minor component of gasoline.

Solvents, such as 2-Me-THF, n-heptane, and iso-propyl acetate, which are being used more frequently as the chemical industry aims to adopt greener, safer, and more sustainable solvents. These spectral tables simplify the identification of these solvents as impurities in NMR spectra following their use in synthesis and workup protocols.

The n-Heptane used in some of Spirits is extremely high purity with very low levels of other organic solvents, heavy metals, and impurities. Blending this high purity n-Heptane with food/pharmaceutical grade Ethanol creates a solvent capable of producing an exceptionally clean, premium quality oil.

n-Heptane is a non-polar solvent that is widely used in several industries such as pharmaceuticals, paints and coatings, electronics, polymer and plastic, adhesives and sealants, textile and industrial cleaning, among others.

n-Heptane is a paint solvent and rubber cement thinner. Heptane is excellent for oil extraction and solvent extraction. Junyuan Petroleum Group produces a high purity (99.9%) grade of n-Heptane. Heptane is widely used in laboratories in the United States as a non-polar solvent. In some botanical processing labs, heptane is used to replace hexane.

The growth of the electronic industry will have a positive impact on the n-Heptane market. Growth of the pharmaceutical industry is also driving the demand for high purity n-Heptane. Also, the rising demand for n-Heptane from other end-use applications such as adhesives & sealants will have a positive impact on the n-Heptane market.

n-Heptane is used as a test fuel constituent. n-Heptane also finds important applications in the purification process of pharmaceutical products and other synthetic organics. n-Heptane and its multiple isomers are extensively used in laboratories as non-polar solvents. As a liquid, n-Heptane is known to display many advantages.

The n-heptane isomerization was conducted at flow unit with an isothermal tubular reactor with fixed bed
catalyst (2 sm3, 0.2-0.7 mm fraction) at a pressure of 1.5 MPa and a temperature range of 140-240ºC. Before the
reaction, the catalyst was reduced in a hydrogen flow at 300 °C for 3 hours, then the reactor was cooled to reaction
temperature and n-heptane was fed with volume velocity of 1h-1) in a Н2/n-heptane ratio =3 (mol.).
Analysis of the reaction products was carried out in the online mode using a gas chromatograph (Tsvet-800)
equipped with a flame ionization detector and capillary column PONA/PIONA (J&W Scientific). The measure of
catalyst activity was the n-heptane conversion . Isomerization selectivity was defined as the ratio of the heptane
isomers sum yield to all isomerization products.

Pt/WO3/ZrO2 Catalysts for n-Heptane Isomerization

POLYSTYRENES (GPPS, HIPS, EPS, SBR, SBS, ABS)

PROPERTIES

Polystyrene (PS) CAS No: 9003-53-6 Polystyrene (PS) is a thermoplastic resin with good processing properties. It is used in many applications including food packaging, domestic appliances, electronic goods, toys, household goods and furniture. The loss of growth in demand for PS has been a major challenge for the industry.
 Expandable Polystyrene (EPS) CAS No: 9003-53-6 Expandable polystyrene (EPS) is a rigid cellular form of polystyrene with good thermal insulation and shock absorbing properties, high compressive strength, very low weight and resistance to moisture.
PS (CAS no. 9003-53-6) is a polymer produced by the polymerization of styrene (CAS no. 100-42-5). There are other polymers in the PS family, such as expandable polystyrene (EPS), rubber-modified polystyrene or high-impact polystyrene (HIPS), which involve other monomers, such as 1,3-butadiene. 

Polystyrene (PS) is a clear, amorphous, nonpolar commodity thermoplastic that is easy to process and that can be easily converted into a large number of semi-finished products like foams, films, and sheets. It is one of the largest volume commodity plastic, comprising approximately seven percent of the total thermoplastic market1. PS is a very good electrical insulator, has excellent optical clarity due to the lack of crystallinity, and has good chemical resistance to diluted acids and bases. It is also easy to fabricate into a large number of finished goods since it is a viscous liquid above its glass transition temperature (Tg) that can be easily molded. However, polystyrene has several limitations. It is attacked by hydrocarbon solvents, has poor oxygen and UV resistance, and is rather brittle, i.e. it has poor impact strength due to the stiffness of the polymer backbone. Furthermore, its upper temperature limit for continual use is rather low due to the lack of crystallinity and its low glass transition temperature of about Tg = 373 K (100°C). Below its Tg, it has medium to high tensile strength (35 – 55 MPa) but low impact strength (15 – 20 J/m). Despite all these weaknesses, styrene polymers are very attractive large-volume commodity plastics.

Some of its weaknesses can be overcome by copolymerization with other monomers. For example, polystyrene can be copolymerized with methyl methacrylate. The copolymer poly(styrene-co-methyl methacrylate) (PSMMA) has higher clarity and improved chemical and UV stability.

One of the most important styrene copolymers is poly(styrene-co-acrylonitrile) (PSAN). It has much improved chemical resistance, better heat stability, and improved mechanical properties. However, these copolymers often yield yellow products.

Probably of equal importance are poly(styrene-co-butadiene) (SBR, SBS) and poly(styrene-co-acrylonitrile-co-butadiene) (ABS). Both copolymers have very high stress and impact resistance and ABS has higher tensile strength than pure PS.

To increase the heat resistance, styrene is sometimes copolymerized with small amounts of maleic anhydride or it is copolymerized with this monomer to an alternating structure. The copolymer poly(styrene-co-maleic anhydride) (PSMA) has a higher Tg than pure polystyrene (400 – 430 K), improved heat resistance and high dimensional stability.

Many styrene derivatives have been synthesized on a laboratory scale and some have been extensively investigated. However, no other styrene polymer has become a large-volume commodity thermoplastic. Among those that are commercially produced are α-methylstyrene, o-, m-, and p-methylstyrene, methoxystyrene, chlorostyrene, divinylbenzene and p-divinylbenzene. The later is used as a cross-linking agent in a large number of different polymer materials.

Polystyrene is a not biodegradable plastic and resistant to photolysis. It is a major contributor to the debris in the ocean. Although recycable, polystyrene is not recycled in many parts of the world. The biggest problem is expandable polystyrene (EPS); due to its low density, it takes up a relative large amount of space in landfills.
In recent years, the (food) packaging industry has developed alternative insulating plastics for thermal applications, like Versalite which is an expanded polypropylene (PP) that can be recycled right along with other PP products in the general recycle stream. We expect other lower-cost and lower-density resins to gain market share in traditional large volume applications of expandable polystyrene.

COMMERCIAL POLYSTYRENES

Polystyrene is one of the most important commodity plastics. The production volume of polystyrene and styrene copolymers is several million tons per year. It is sold under various trade names, including Styrofoam™, Styropor®, and Styron™

The three most important grades of styrene are:

GPPS: General purpose polystyrene, also known as crystal-clear polystyrene, is a fully transparent, rigid and rather brittle low cost thermoplastic made from styrene monomer. GPPS is a solid product manufactured in the form of 2-5 mm pellets.

HIPS: High impact polystyrene contains usually 5 to 10% rubber (butadiene) and is used for parts which require high(er) impact resistance. HIPS is a graft copolymer having polystyrene sidearms. The grafting occurs when some of the radicals react with the double bonds of the polybutadiene.

EPS: Expandable polystyrene consists of micro-pellets or beads containing a blowing agent (usually pentane). The expanded or foamed polystyrene is thermally insulating, has high impact resistance and good processability.

Styrenic Copolymers and their blends are considered engineering thermoplastics because their properties can be tailored over a wide range for a large number of applications with a broad range of processing methods which permits the manufacture of high quality, very durable plastic products suitable for many demanding applications.

APPLICATIONS

Polystyrene is a polymer that is cheap and easy to process. It is the material of choice for many applications including food-packaging, disposable consumer plastic goods as well as parts for optical, electronic/electrical, and medical applications. A large variety of products are formed by injection molding including dining utensils, plastic cups, housewares, toys, CD cases, cosmetic containers, covers and fixtures.

Expandable polystyrene, either crystal polystyrene2 or styrene copolymers soaked with a blowing agent (usually pentane), are used to produce various foamed products, like disposable drinking cups, egg cartons, trays, fast-food containers, cushioned packaging, and thermal insulation for the construction market.

Medical applications include pipettes, Petri dishes and medicine containers.

Pentane is used for Polystyrene Production

Industry Information

Expanded Polystyrene, EPS, This is a special grade consisting of spherical beads of a blend of polystyrene-polyphenylene ether containing pentane as expansion agent, typically used for medium density foam with improved thermal resistance. Pentanes – aliphatic hydrocarbon solvents. Junyuan Petroleum Group of Companies are leading suppliers of Pentanes, a group of high purity aliphatic hydrocarbon solvents that comprises normal- and iso-Pentane and blends of the two components.
Pentane is introduced to suspension-polymerised polystyrene (PS) beads. Molecular weights in the range of 150,000–250,000 are used (see Section 4.4.2 ). The spherical beads are sieved to a narrow range of diameters, so are not monodisperse.

Pentane
Pentane is used mainly as a blowing agent, a liquid substance that when applied takes shape into a harder material used to make polystyrene foam. Pentane is also a blend for gasoline.

Pentanes Plus
Pentanes Plus is a mixture of mostly pentane combined with isopentane, natural gasoline and plant condensate. Pentanes Plus is used as a gasoline blend and in heavy oil sands blending as a diluent, to ship heavy crude oil by pipeline.

Isobutane
Isobutane, among other things, is used for gasoline blending, as a propellant for aerosols and as a refrigerant.


Contact us to buy. With a narrow boiling range, consistent composition and fast evaporation Pentanes are primarily used as propellants in aerosols, as blowing agents in foams (eg expandable polystyrene)


Polystyrene Manufacturers

Polystyrene is an aromatic polymer commercially derived from the petroleum based monomer, styrene. Abbreviated PS, this particular plastic is ubiquitous in daily life, second in use only to polyethylene. Polystyrene exhibits the same strength as unalloyed aluminum, but is much lighter and offers significantly increased flexibility.

Desirable properties such as good thermal and electrical insulation, resistance to acids, alkalis, oils and alcohols in addition to being lightweight and flexibility, makes polystyrene products a popular and economic choice for a broad array of industries. Packaging, building, construction and architectural design make frequent use of this material. Furthermore, polystyrene is chemically non-reactive, making its use popular in food, medical, biomedical and pharmaceutical industries as well as applications involving the storage of volatile chemicals. Products produced for such uses are often sterilized by irradiation or an ethylene oxide treatment. Electronic housings, compact discs, cutlery, beakers, insulating panels, food trays, packaging products and window panels are just a few of the myriad polystyrene products available to accommodate the broad spectrum of industrial, commercial and residential use. A thermoplastic, PS is pliable when heated and rigid when cold allowing it to be easily recycled and remolded numerous times. As it is non-biodegradable, diligent recycling is essential to diminishing the environmental impact of this plastic material.

The many uses of polystyrene all begin with the same process of joining monomers to create the plastic polymers. Classified as a liquid hydrocarbon, PS is composed of the elements hydrogen and carbon. Through the free-radical polymerization of petroleum or the derivative phenylethene (another name for styrene), and using benzoyl peroxide as the initiator, these hydrocarbon monomers form covalent bonds with phenol groups to create polystyrene. Beyond this point polystyrene can be manufactured in a number of different ways. The most recognizable pre-form of polystyrene is the trade marked extruded foam, Styrofoam. Also available in expanded foam, moldable solids or viscous fluids, polystyrene is supplied to hundreds of different industries in the most applicable pre-form. Injection molding, casting, extrusion and stamping are used to manufacture products from this dimensionally stable material. Polystyrene manufacturers fabricate a diverse range of stock forms which may include plastic rods, plastic sheets, plastic films, pipes, tubes, plates and more. These may be utilized as finished products or can be processed further to satisfy particular specifications. In solid form, polystyrene is a colorless, glass-like rigid material. Polystyrene softens just above 100 degrees Celsius and becomes viscous at 185 degrees Celsius. Different fillers can be added to molten polystyrene during processing to alter porosity, strength, flexibility and thermal capabilities.

The Difference Between Hexane and Heptane

The Difference Between Hexane and Heptane

Hexane vs. Heptane

Hexane and Heptane are similar hydrocarbon mixtures that have several important differences.

Key Differences

  • Heptane is less toxic and less volatile than Hexane
  • The low toxicity of Heptane makes it a safer chemical alternative than Hexane for gasoline and other applications.
  • Hexane’s lower viscosity than Heptane enables it to be utilized for a wider variety of solvent applications than Heptane.

Shared Applications

Hexane and Heptane are similar enough that they can be used interchangeably for certain applications.

  • Heptane and Hexane are both found in gasoline and have a gasoline-like odor.
  • Heptane and Hexane both have vapors that are heavier than air.
  • Hexane and Heptane are both insoluble in water, which is likely due to the fact that both are non-polar solvents.
  • The fact that both Hexane and Heptane are non-polar solvents is derived from their shared status as hydrocarbon molecules.
  • Non-polar solvents are able to dissolve other non-polar solvents. This is a quality shared by both Hexane and Heptane and why they are useful to extract oils and greases.
  • Heptane and Hexane are both utilized as industrial cleaners, because of their powerful solvency.
  • Heptane and Hexane can both be used for chromatography, which is the laboratory process of separating mixtures.

Common Uses

As previously stated, Heptane and Hexane are both components of gasoline. However, these substances have other unconventional uses in popular consumer items.

Hexane is an indirect additive to soy-based food products, because it is used to extract oils from plant seeds such as soy beans, corn, sun-flowers, and canola.

It is less expensive to extract oil with Hexane, than it is to use the traditional method of pressing oils out of seeds.

It is possible for Hexane residue to be left in soy-based foods and other materials, but it is unlikely for Hexane residue to be toxic in food items.

Using Hexane to extract soybean oil is often both cost-efficient, and energy efficient as opposed to other methods of extraction.

Pure Hexane is not used to extract soybean oil, but rather a mixture of isomers that comprise Commercial grade Hexane.

Hexane is also used for extraction of vitamin E from certain foods, however Heptane can also be used for this purpose and is a much safer alternative.

Heptane is effective at separating vitamin E from cereal products without the potential harm associated with Hexane.

Heptane is also utilized as an outdoor oven cleaner.

Either Heptane or Hexane can be found in rubber cement along with minor components of IPA 99%, acetone, or toluene.

Purchase n-Heptane, n-Hexane or Isohexane high purity solvents produced by Junyuan Petroleum Group, or if you have questions, please email us at info@junyuanpetroleumgroup.com or call us at +86 178 1030 0898 to speak with one of our knowledgeable sales representatives. We welcome the opportunity to answer any questions you may have or assist you with a quote. We welcome the opportunity to answer any questions you may have or assist you with a quote.

 

Isopentane vs Pentane – What’s the difference?

Isopentane vs Pentane – What’s the difference?

As nouns the difference between isopentane and pentane
 is that isopentane is (organic compound) the aliphatic hydrocarbon ; isomeric with pentane and neopentane while pentane is (organic compound) an aliphatic hydrocarbon of chemical formula c5h12; either of the three isomers n-pentane, methyl-butane (isopentane), and di-methyl-propane (neopentane); volatile liquids under normal conditions.

Definitions of n-Pentane:
-CAS Number: 109-66-0. A clear, colorless solution with a mild, gasoline-like odor. It is used in natural gas, lighter fluid, blowtorch fuels, and aerosol propellants. Chemical formula = C5H12. Molecular weight = 72.15 g/mol.
-Pentane also known as amyl hydride or skellysolve is an alkane hydrocarbon with the chemical formula CH3(CH2)3CH3. 3 isomers exist for pentane: n-pentane (linear molecule), isopentane (2-methylbutane) and neopentane which is formally 2,2-dimethylpropane.

Definitions of Isopentane:
Isopentane, also called methylbutane or 2-methylbutane, is an organic chemical compound which is one of the three pentane isomers. Isopentane is a branched-chain alkane with five carbon atoms. Isopentane is an extremely volatile and extremely flammable liquid at room temperature and pressure. The normal boiling point is just a few degrees above room temperature and isopentane will readily boil and evaporate away on a warm day.

Isopentane Depositor-Supplied Synonyms
ISOPENTANE
2-Methylbutane
78-78-4
Isoamylhydride
Butane, 2-methyl-
iso-Pentane
1,1,2-Trimethylethane
Dimethylethylmethane
Ethyldimethylmethane
1,1-dimethylpropane
ISO PENTANE
Butanes
iso-C5H12
NSC 119476
UNII-ZH67814I0O
HSDB 618
EINECS 201-142-8
AI3-28787
(CH3)2CH-CH2-CH3
CHEBI:30362
ZH67814I0O
2-Methylbutane, for HPLC
Q-200305
2-Methylbutane, 99+%, for spectroscopy
2-Methylbutane, ReagentPlus(R), >=99%
2-Methylbutane, 99+%, Extra Dry, AcroSeal(R)
Mixed butanes
Field butane
2-methyl-butane
solvent isopentane
95% isopentane
99% isopentane
C7-8 isoparaffin
Butane (petroleum)
Propane, dimethyl-
Exxsol isopentane S
1,2-Trimethylethane
Butane (field grade)
blowing agent isopentane
ACMC-209pfa
foaming agent Isopentane
C3-C4 Splitter bottoms
Mixed butanes (petroleum)
isopentane(2-methylbutane)
EC 201-142-8
KSC155C9N
UNII-53X7V89P1E
CHEMBL1797287
DTXSID8025468
CTK0F5196
R-601a
53X7V89P1E
WLN: 2Y1&1
2-Methylbutane, SAJ special grade
2-Methylbutane, analytical standard
Butane-isobutane stream (petroleum)
ZINC1709041
EINECS 271-009-7
EINECS 274-273-1
2-Methylbutane, 99+%, extra pure
2-Methylbutane, anhydrous, >=99%
ANW-37220
MFCD00009338
NSC119476
AKOS015841718
FCH1112917
LS-1753
MCULE-5376105936
NSC-119476
KS-00000X66
2-Methylbutane, for HPLC, >=99.5%
2-Methylbutane, purum, >=95.0% (GC)
M0167
NS00003083
2-Methylbutane, SAJ first grade, >=99.0%
15415-EP2270008A1
15415-EP2287153A1
15415-EP2292589A1
15415-EP2292617A1
15415-EP2305683A1
15415-EP2311808A1
15415-EP2311829A1
15415-EP2311839A1
15415-EP2314574A1
15415-EP2314589A1
15415-EP2316837A1
15415-EP2372804A1
15415-EP2378585A1
92812-EP2295417A1
92812-EP2305649A1
92812-EP2380568A1
2-Methylbutane, puriss. p.a., >=99.5% (GC)
2-Methylbutane, spectrophotometric grade, >=99%
212698-EP2374780A1
212698-EP2374781A1
Q422703
Isopentane Solution, Pharmaceutical Secondary Standard; Certified Reference Material
1320-76-9
61G

Geothermal Energy Powers New Zealand


Geothermal power development in New Zealand first began in the mid-1950s, and there is the potential for the supply of up to ten per cent of the country’s power needs. New Zealand already has over 300 MW of installed geothermal capacity. In recent years, deregulation of the power industry has encouraged further development, and two new plants entered commercial operation late last year.


The original settlers of New Zealand, the Maoris, who arrived around 800 years ago from the central Pacific, used the natural geothermal springs for bathing and the very hot springs and geysers for cooking. Now the country uses this natural energy to supply around three per cent of its power needs, and is seeking to further develop its potential.

New Zealand is on the south-west corner of the Pacific “ring of fire”, the chain of volcanic activity which extends up through the Pacific Islands, Indonesia, the Philippines, Japan, Alaska, the west coast of the USA, and down to the tip of South America. This volcanic activity arises from weaknesses in the earth’s crust where the Pacific tectonic plate meets neighbouring plates.

There have been a number of major volcanic eruptions in the region, the most recent being the Tarawera eruption of 1856 and the largest being the eruption which formed Lake Taupo around 400 AD. The ancient Chinese recorded the impact of the ash emitted by the latter on their weather. Where there is volcanic activity there are often geothermal fields capable of commercial development for power generation.

New Zealand was one of the early developers of geothermal power with the Wairakei project being the first large scale development of a water dominated geothermal field in the mid-1950s. There has been a second phase of geothermal development since the mid-1980s, stimulated largely by deregulation of the electricity industry which allowed the distribution companies to be more active in generation development.

There is geothermal activity spread over both islands of New Zealand with the main high temperature fields of volcanic origin in the Rotorua-Taupo area in central North Island. Most of the other geothermal activity in the country is of tectonic origin and the heat flows and temperatures are not sufficient for commercial power generation.

Early developments

The first geothermal fields to be developed were Kawerau and Wairakei in the Rotorua-Taupo area. The Kawerau field is 20 km inland from the town of Whakatane and is the site of New Zealand’s first pulp and paper mill. Here, geothermal steam is used directly in the mill for paper drying and for boiler feedwater heating as well as for electricity generation. The wells produce two phase geothermal fluid which is flashed to produce steam leaving the brine to be discharged to the ground. More recently some reinjection wells have been drilled and there is a programme to introduce full reinjection. Despite 40 years of abstraction, the field has maintained a good pressure and should have many years of further life.

In 1989 the local power company, Bay of Plenty Electricity, installed an Ormat binary plant of two units with an output of 2.2 MW (known as TG1) to utilise the energy in the 172°C brine from one of the wells. This was followed in 1993 by a second Ormat unit of 3.6 MW (known as TG2) on a separate brine flow. Both units utilise isopentane as the working fluid and are air cooled.

Wairakei, 9 km to the north of Taupo and first commissioned in 1959, was the first major geothermal power station in New Zealand. The Wairakei geothermal field consists of a pumiceous pyroclastic reservoir underlain by ignimbrites and capped by lacustrine mudstone. The upflow temperature is 270°C with typical production temperatures of 230°C. The wells generally produce two phase flow, with dry steam in some areas. This was the first wet geothermal field in the world to be utilised for commercial power production.

Their are two stations at Wairakei utilising steam at intermediate pressure (3.5 bar) and low pressure (0.1 bar). The current net output is 153 MW and the annual energy production 1300 GWh. Originally there were high pressure (12.6 bar) turbines as well, but these were moved to Ohaaki when the reservoir pressure declined. The station design originally incorporated a heavy water plant for the British nuclear programme, but this was dropped before construction.

However, the Wairakei power station is a major source of contaminants in the Waikato River. Around 1100 t/h of steam is condensed in the turbines’ spray condensers which use the river water directly, and around 3500 t/h of brine is discharged to streams which flow to the river. A programme is therefore underway to reinject the brine and the feasibility of further generation from the brine energy is also under review.

In response to the oil crises of the 1970s, the government investigated and drilled most of the known geothermal fields in the Taupo-Rotorua area. Many of these showed commercial potential and the 13 km2 Broadlands field was selected for the development of the Ohaaki geothermal station. This station is owned and operated by Contact Energy, one of the two state-owned generating companies, which operates the station remotely from its other geothermal station, Wairakei.

A total of 51 wells with an average depth of 1000 m were drilled, and a 103 MW station was completed in 1989. The 24 production wells produce two phase fluid which is separated to a steam flow for the power station and a brine flow which is pumped to eight reinjection wells. The 12.5 bar steam is fed to two 11.5 MW back pressure turbines which were originally installed at Wairakei. Steam from these turbines at 3.5 bar, supplemented by low pressure steam from the wells, supplies two 47 MW Mitsubishi condensing turbines.

Ohaaki was the first large scale reinjection of brine in New Zealand and the first use of a concrete natural draught cooling tower. Due to field pressure decline the station now operates at 80 MW giving an annual energy production of around 750 GWh. Despite the reinjection of brine and condensate, there has been considerable subsidence in parts of the steam field and areas adjacent to the Waikato River.

New capacity

The McLachlan power station, located about 5 km from Taupo, is the first privately owned power station in New Zealand and has been developed by a joint venture of a Taupo businessman and the Auckland electricity distribution company Mercury Energy. These partners have taken an unconventional approach in order to reduce the capital costs – it can be hard to reach financial closure for a geothermal project in New Zealand’s wholesale market.

The power plant is sited on one edge of the Wairakei geothermal field, and is drawing from the same resource as the Wairakei geothermal station. In that area of the field there is a relatively shallow steam cap and the station takes dry steam from four wells of around 750 m depth. The total project cost was $57 million (NZ$81 million) and full commercial production started in June 1997.

Because the station draws from a resource utilised by an existing station there were considerable difficulties in obtaining the necessary planning consents. The consents to draw steam were granted under the now repealed Geothermal Energy Act following protracted negotiations with the government-owned generating company and public hearings. The consents to draw steam are not sufficient to operate the station at the full output of 53 MW, and the station operates at minimum load during the night when electricity market prices are at their lowest levels and at full output during the day. There were also problems with obtaining the air discharge consents when a local group appealed the consents granted, resulting in a six month delay in project commissioning.

The McLachlan plant has a single 55 MW gross output Fuji condensing turbine of conventional design including an underslung shell and tube condenser and a hydrogen cooled generator. This gives a turbine hall configuration very similar to any other steam unit, with the operating floor high above ground. The turbine and generator were originally destined for a station on the Geysers geothermal field in California, but were never installed due to the over exploitation of the field and consequent pressure decline becoming apparent before the installation commenced.

The unit was stored under controlled conditions for a number of years and refurbished for 50 Hz operation and the lower steam pressure before shipment to New Zealand. This mainly involved changes to the turbine blades and the installation of a much larger non-condensable gas extraction system. Cooling takes place by conventional mechanical draught cooling towers, with the condensate used as tower make-up water. The blow down from the cooling towers and any excess condensate is pumped 2 km to a shallow well.

As part of the de-rating from 3600 r/min to 3000 r/min for 50 Hz operation, the generator voltage was reduced to 11 kV allowing use of standard New Zealand switchgear. The generator output is stepped up to 220 kV and fed into the Wairakei-Whakamaru 220 kV line, which is part of the National Grid, by a short simple Tee connection.

The turbine and generator came with only the control systems closely associated with their operation, and a new computer based overall station control system employing sophisticated graphic interfaces has been installed. Considerable work was necessary to uprate and adapt the electrical auxiliary systems to meet the current design codes, particularly as relates to the hazardous areas around the hydrogen cooling systems. The station is manned at all times, and all the maintenance work will be carried out by contract.

By utilising a second hand refurbished plant and new auxiliary and control systems, the joint venture has been able to complete the station with full manufacturers warranties at a considerably lower capital cost than if new plant had been utilised. The full engineering of the station and the detailed design of the changes to pipe work and the electrical systems was undertaken by the New Zealand consultant HPM Power.

The Rotokawa geothermal field is a deep high-temperature field covering 25 km2 and located 12 km north of Taupo. The surface manifestations of the field include small hot springs and an acidic lake which contains large quantities of colloidal sulphur from the oxidation of hydrogen sulphide as it bubbles to the surface. Eight wells were drilled between 1966 and 1986 as part of the government’s programme to assess the region’s geothermal resources. Most of these have since been capped and abandoned, either because they were not commercial producers or because of casing corrosion. The field has an estimated capacity of 100 to 200 MWe, and is being developed by a 24 MW station in order to allow careful monitoring of the resource before full exploitation.

The project is unique as it involves the participation of the indigenous Maori people in the development as a joint venture partner with Auckland electricity distributor Power New Zealand. The Tauhara North No. 2 Trust owns the land over the middle of the geothermal field, including the land around the well RK5 which is the best of the wells drilled by the government.

The project has two production wells of around 2000 m depth producing two phase fluid which is piped to a separator at the station. Steam is separated from the brine at 23 bar and both streams are used for electricity generation. The condensed steam is pumped up to the brine pressure, combined with the high pressure brine, and reinjected with no further pumping. There are three reinjection wells of 500 m depth, one of which is one of the original field exploratory wells.

In the process of selecting a turnkey contractor for the power station, the alternatives of condensing steam turbines and binary plant were compared. The plant finally selected is configured to use steam turbine and binary plant, and obtain the best of both technologies. The contractor for the 24 MW plant is Ormat Industries Ltd. of Israel.

To maximize the benefits of the high steam pressure, a back pressure turbine of 12 MW output is utilised to drop the steam pressure to 1.5 bar. This low pressure steam is condensed in two binary units of 4 MW output each. This configuration, called a “geothermal combined cycle unit” by Ormat, has the advantage of the low capital cost of a simple back pressure turbine and of condensing the steam in a heat exchanger where steam wetness is not a problem. There is a third binary unit also of 4 MW output utilising the hot brine flow, cooling it from 219°C to 150°C. The motive fluid in the binary units is isopentane and cooling is by air radiators.

Future development

There are a number of geothermal fields at various stages of development and some projects may proceed despite the low wholesale electricity prices, which are averaging around 3.0 c/kWh. In the far north the Ngawha field is being developed with an initial 8 MW Ormat binary plant due for commissioning in early 1998. The Mokai field is probably the best geothermal field in New Zealand with an output of 200 to 400 MWe. A contract has also been awarded to Ormat for a 50 MW plant of similar configuration to Rotokawa, and finance is now being finalized.

Resource use and planning consents have been granted for drilling the Rotoma and Taheke fields near Rotorua and have been filed for the Tauhara field near Taupo. There are also proposals to further develop the Kawerau field. Geothermal energy has met around three per cent of New Zealand’s electricity needs for many years, and has the potential to supply up to ten per cent. However, major impediments exist, including an excess of generating capacity in the short term leading to low wholesale electricity prices, and difficulties in obtaining the necessary planning and resource consents.

Eastland Group in New Zealand announces having entered the commissioning phase for its 25 MW Te Ahi O Maui geothermal power plant. With that New Zealand enters the 1 GW Geothermal Country club of countries that have an installed power generation capacity of more than 1,000 MW (1 GW).

Countdown to Te Ahi O Maui ‘go live’

  • July 2014: Resource consents are awarded to Te Ahi O Maui.
  • September 2015: Decision to proceed is signed off by Eastland Community Trust.
  • January 2016: Construction of project roads commences with Eastern Bay of Plenty contractor Grant Farms Ltd. Well pad construction is undertaken by Seay Earthmovers from Taupo.
  • May 2016: After assembly, inspections and karakia and blessings from the local kaumatua, drilling begins with MB Century and Halliburton. Ormat is engaged for the construction of the plant.
  • June 2016: Earthworks for the power plant and separator get underway with Seay Earthmovers.
  • Early 2017 onwards: Ormat mobilises to site to begin the foundation works for the power plant. Construction continues throughout 2017. MB Century is awarded the contract for the design and construction of the steamfield. Horizon Contracting, part of the electricity distribution company in the Bay of Plenty, constructs the transmission line.
  • September 2018: Plant construction is complete, and commissioning with Ormat begins. There will be a string of tests to ensure that the plant and all systems operate correctly, followed by a reliability run.
  • October 2018: Ormat is due to formally hand over Te Ahi O Maui to begin full commercial operations.
Dieng geothermal field, Indonesia

Isopentane, CAS No.:78-78-4, Chemical Formula:C5H12, SynonymsButane, 2-methyl-; iso-Pentane; 1,1,2-Trimethylethane; 2-Methylbutane; iso-C5H12; Ethyldimethylmethane; Isoamylhydride; Junyuan isopentane; 1,1-dimethylpropane; methylbutane; Iso-Pentane * Isopentane; Junyuan isopentane S; NSC 119476

Isopentane #ISOPentane #methylbutane #2methylbutane # C5H12 #C5H2 #CAS78784

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Darajat III geothermal plant, Indonesia

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