SU1428209A3 - Method of producing carburettor engine fuel - Google Patents
Method of producing carburettor engine fuel Download PDFInfo
- Publication number
- SU1428209A3 SU1428209A3 SU853866458A SU3866458A SU1428209A3 SU 1428209 A3 SU1428209 A3 SU 1428209A3 SU 853866458 A SU853866458 A SU 853866458A SU 3866458 A SU3866458 A SU 3866458A SU 1428209 A3 SU1428209 A3 SU 1428209A3
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- vergaserkraftstoff
- wird
- und
- daß
- benzolgehalt
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
- C10L1/06—Liquid carbonaceous fuels essentially based on blends of hydrocarbons for spark ignition
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Liquid Carbonaceous Fuels (AREA)
Abstract
Description
СлSl
Ивобретение относитс к способу получени топлива, в частности карбюраторного топлива из легких нефтепродуктов ожижени угл .The invention relates to a method for producing fuel, in particular carburetor fuel from light petroleum liquefying coal.
Целью изобретени вл етс повы- шение качества топлива за счет снижени степени его вредности путем уменьшени содержани бензола.The aim of the invention is to improve the quality of the fuel by reducing its harmfulness by reducing the benzene content.
Пример 1. 100 мае.ч. про- дукта риформинга с пределами кипени AO-ZOS C, октановым числом по исследовательскому (моторному) методу 99,3 (98,0) и с содержанием бензола 12 мас.%, полученного путем гидро- очистки продуктов ожижени угл с Прделами кипени 20-400 С при 400 С и давлении 280 бар на торговом ко- бальтово-молибденовом катализаторе гидрировани , отделени ректификади- ей из продукта гидроочистки фракции с пределами кипени 40-205 С и последующего катализатора риформинга при температуре 490 С и давлении 23 бар на платиновом катализаторе, на у -окиси алюмини (1,64 мас.% платины ), содержащей также 1,8 мас.% хлора, подвергают ректификации в 15- тарельчатой насадочной колонне при флегмовом числе 1:2, причем получают фракцию с пределами кипени 65-85°С, которую в качестве бокового потока .отвод т из колонны в количестве 19 мае.ч. Боковой поток имеет следующий состав, мас.%: бензол 49,4i вые шие изомерные парафины 20,5; метил- циклопентан 12,2; н-гексан 9,8{ гомологи циклопентаново го р да 7,0; циклопентан 1,1. Получаемые на ректификации головной продукт (11 мае.ч., конец .кипени 65 С) и кубовый продукт (70 мае.ч., начало кипени 85 с) объедин ют и в качестве целевого продукта отвод т из процесса.Example 1. 100 mach. of the reforming product with the boiling range AO-ZOS C, the octane number by the research (motor) method 99.3 (98.0) and with a benzene content of 12% by weight, obtained by hydro-purifying the coal liquefaction products with a Prdel of 20- 400 C at 400 C and a pressure of 280 bar on a commercial cobalt-molybdenum catalyst for hydrogenation, separation of the fraction with a boiling point of 40–205 C and a subsequent reforming catalyst at a temperature of 490 C and a pressure of 23 bar on a platinum catalyst, by distillation from the hydrotreating on γ-alumina (1.64 wt.% platinum ), which also contains 1.8% by weight of chlorine, is subjected to rectification in a 15-plate packed column at a reflux ratio of 1: 2, and a fraction with boiling limits of 65-85 ° C is obtained, which as a side stream is removed from the column the amount of 19 ma.ch. The side stream has the following composition, wt%: benzene 49.4i; the resulting isomeric paraffins 20.5; methyl cyclopentane 12.2; n-hexane 9.8 {homologues of the cyclopentane row 7.0; cyclopentane 1.1. The head product obtained on rectification (11 wt. Parts, boiling end 65 C) and bottom product (70 parts by weight, boiling point 85 seconds) are combined and withdrawn from the process as a desired product.
Получаемое таким образом бедное бензолом карбюраторное топливо имеет октановое чиело по иеследовательском ( моторному) методу, равное 100 (89). IThe carburetor fuel, which is poor in benzene in this way, has an octane rating according to the research (motor) method of 100 (89). I
Пример 2. Повтор ют пример Example 2. Repeat example
с той розницей, что из продукта риформинга ректификацией отдел ют в качестве бокового Потока фракцию с пределами кипени 70-81 С. Получаемое при этом карбюраторное топливо имеет октановое число по исследовательскому (моторному) методу, равное .95 (85).with the retail that the fraction with a boiling range of 70-81 C is separated from the reforming product as a sidestream, the fraction obtained from the carburetor fuel has an octane rating of (95) according to the research (motor) method.
Claims (1)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19843410455 DE3410455A1 (en) | 1984-03-22 | 1984-03-22 | METHOD FOR PRODUCING A GASIFYING FUEL FROM CARBON OIL |
Publications (1)
Publication Number | Publication Date |
---|---|
SU1428209A3 true SU1428209A3 (en) | 1988-09-30 |
Family
ID=6231228
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU853866458A SU1428209A3 (en) | 1984-03-22 | 1985-03-18 | Method of producing carburettor engine fuel |
Country Status (9)
Country | Link |
---|---|
EP (1) | EP0155456B1 (en) |
JP (1) | JPS60212489A (en) |
BR (1) | BR8501232A (en) |
CA (1) | CA1237087A (en) |
DD (1) | DD232306A5 (en) |
DE (2) | DE3410455A1 (en) |
PL (1) | PL145199B1 (en) |
SU (1) | SU1428209A3 (en) |
ZA (1) | ZA852076B (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3502062A1 (en) * | 1985-01-23 | 1986-07-24 | Veba Oel Entwicklungs-Gesellschaft mbH, 4650 Gelsenkirchen | CARBURETOR FUEL AND METHOD FOR PRODUCING THE SAME FROM CARBON OIL |
BRPI0809289A2 (en) | 2007-03-19 | 2014-10-14 | Sued Chemie Ag | GENERATION OF CHEMICAL CONSTRUCTION BLOCKS FROM VEGERAL BIOMASS BY SELECTIVE DEPOLYMERIZATION |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1041727B (en) * | 1956-11-29 | 1958-10-23 | Bataafsche Petroleum | Motor fuel |
US3518182A (en) * | 1968-03-29 | 1970-06-30 | Chevron Res | Conversion of coal to liquid products |
DE3213220A1 (en) * | 1982-04-08 | 1983-10-13 | Ruhrkohle Ag, 4300 Essen | CARBURETOR FUEL |
-
1984
- 1984-03-22 DE DE19843410455 patent/DE3410455A1/en active Granted
-
1985
- 1985-01-18 DD DD85272645A patent/DD232306A5/en unknown
- 1985-01-22 DE DE8585100616T patent/DE3564962D1/en not_active Expired
- 1985-01-22 EP EP85100616A patent/EP0155456B1/en not_active Expired
- 1985-03-06 JP JP60042775A patent/JPS60212489A/en active Granted
- 1985-03-18 SU SU853866458A patent/SU1428209A3/en active
- 1985-03-20 BR BR8501232A patent/BR8501232A/en not_active IP Right Cessation
- 1985-03-20 ZA ZA852076A patent/ZA852076B/en unknown
- 1985-03-21 PL PL1985252488A patent/PL145199B1/en unknown
- 1985-03-21 CA CA000477085A patent/CA1237087A/en not_active Expired
Non-Patent Citations (1)
Title |
---|
Башилов А.А. и др. Компаундирование моторных топлив. М., 1958, с. 53-54. Lviger. Lexikon der Technik, 1965, Bd6. * |
Also Published As
Publication number | Publication date |
---|---|
PL252488A1 (en) | 1985-11-19 |
PL145199B1 (en) | 1988-08-31 |
ZA852076B (en) | 1985-11-27 |
JPS60212489A (en) | 1985-10-24 |
DE3410455A1 (en) | 1985-10-03 |
BR8501232A (en) | 1985-11-12 |
EP0155456A3 (en) | 1987-01-21 |
EP0155456A2 (en) | 1985-09-25 |
CA1237087A (en) | 1988-05-24 |
JPH0451598B2 (en) | 1992-08-19 |
DE3410455C2 (en) | 1987-10-15 |
DE3564962D1 (en) | 1988-10-20 |
DD232306A5 (en) | 1986-01-22 |
EP0155456B1 (en) | 1988-09-14 |
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