FI59810C - Foerfarande foer framstaellning av braensle foer jetmotor - Google Patents
Foerfarande foer framstaellning av braensle foer jetmotor Download PDFInfo
- Publication number
- FI59810C FI59810C FI2312/72A FI231272A FI59810C FI 59810 C FI59810 C FI 59810C FI 2312/72 A FI2312/72 A FI 2312/72A FI 231272 A FI231272 A FI 231272A FI 59810 C FI59810 C FI 59810C
- Authority
- FI
- Finland
- Prior art keywords
- feedstock
- hydrogenation
- zone
- hydrogenation zone
- hydrogen
- Prior art date
Links
- 238000005984 hydrogenation reaction Methods 0.000 claims description 42
- 238000000034 method Methods 0.000 claims description 36
- 239000001257 hydrogen Substances 0.000 claims description 33
- 229910052739 hydrogen Inorganic materials 0.000 claims description 33
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 29
- 239000007788 liquid Substances 0.000 claims description 24
- 239000000446 fuel Substances 0.000 claims description 23
- 239000007789 gas Substances 0.000 claims description 23
- 229930195733 hydrocarbon Natural products 0.000 claims description 20
- 150000002430 hydrocarbons Chemical class 0.000 claims description 20
- 239000007791 liquid phase Substances 0.000 claims description 15
- 239000012071 phase Substances 0.000 claims description 14
- 238000009835 boiling Methods 0.000 claims description 13
- 239000004215 Carbon black (E152) Substances 0.000 claims description 11
- 239000003054 catalyst Substances 0.000 claims description 9
- 239000000295 fuel oil Substances 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 6
- 150000003464 sulfur compounds Chemical class 0.000 claims description 5
- 239000012535 impurity Substances 0.000 claims description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 3
- 229910052717 sulfur Inorganic materials 0.000 claims description 3
- 239000011593 sulfur Substances 0.000 claims description 3
- 238000006243 chemical reaction Methods 0.000 description 11
- 239000000203 mixture Substances 0.000 description 10
- 238000000926 separation method Methods 0.000 description 8
- 150000002431 hydrogen Chemical class 0.000 description 5
- 238000004517 catalytic hydrocracking Methods 0.000 description 4
- 239000003208 petroleum Substances 0.000 description 4
- 239000000779 smoke Substances 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 125000003118 aryl group Chemical group 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 2
- 238000009903 catalytic hydrogenation reaction Methods 0.000 description 2
- 238000005194 fractionation Methods 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 239000012263 liquid product Substances 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 239000005909 Kieselgur Substances 0.000 description 1
- 239000007868 Raney catalyst Substances 0.000 description 1
- 229910000564 Raney nickel Inorganic materials 0.000 description 1
- 230000002730 additional effect Effects 0.000 description 1
- 230000029936 alkylation Effects 0.000 description 1
- 238000005804 alkylation reaction Methods 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 235000019568 aromas Nutrition 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000012455 biphasic mixture Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 230000007123 defense Effects 0.000 description 1
- 238000006356 dehydrogenation reaction Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 229910052809 inorganic oxide Inorganic materials 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 230000000391 smoking effect Effects 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
- B01J8/0446—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
- B01J8/0449—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds
- B01J8/0453—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds the beds being superimposed one above the other
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/08—Jet fuel
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Liquid Carbonaceous Fuels (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US17736271A | 1971-09-02 | 1971-09-02 | |
| US17736271 | 1971-09-02 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| FI59810B FI59810B (fi) | 1981-06-30 |
| FI59810C true FI59810C (fi) | 1981-10-12 |
Family
ID=22648306
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| FI2312/72A FI59810C (fi) | 1971-09-02 | 1972-08-21 | Foerfarande foer framstaellning av braensle foer jetmotor |
Country Status (11)
| Country | Link |
|---|---|
| US (1) | US3767562A (enExample) |
| JP (1) | JPS5442005B2 (enExample) |
| AU (1) | AU469380B2 (enExample) |
| CA (1) | CA983420A (enExample) |
| DE (1) | DE2242331A1 (enExample) |
| ES (1) | ES406277A1 (enExample) |
| FI (1) | FI59810C (enExample) |
| FR (1) | FR2151059B1 (enExample) |
| GB (1) | GB1399108A (enExample) |
| IT (2) | IT962225B (enExample) |
| NL (1) | NL176583C (enExample) |
Families Citing this family (38)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA1033680A (en) * | 1973-07-12 | 1978-06-27 | Lummus Company (The) | Production of jet fuel |
| US4427534A (en) | 1982-06-04 | 1984-01-24 | Gulf Research & Development Company | Production of jet and diesel fuels from highly aromatic oils |
| US4849093A (en) * | 1987-02-02 | 1989-07-18 | Union Oil Company Of California | Catalytic aromatic saturation of hydrocarbons |
| US5183556A (en) * | 1991-03-13 | 1993-02-02 | Abb Lummus Crest Inc. | Production of diesel fuel by hydrogenation of a diesel feed |
| DE4235450A1 (de) * | 1991-11-05 | 1993-05-06 | Rieter Ingolstadt Spinnereimaschinenbau Ag, 8070 Ingolstadt, De | Verfahren und vorrichtung zum ermitteln des durchmessers einer spule an einer spinnstelle einer spinnmaschine |
| US5393408A (en) * | 1992-04-30 | 1995-02-28 | Chevron Research And Technology Company | Process for the stabilization of lubricating oil base stocks |
| US6296757B1 (en) | 1995-10-17 | 2001-10-02 | Exxon Research And Engineering Company | Synthetic diesel fuel and process for its production |
| US5689031A (en) | 1995-10-17 | 1997-11-18 | Exxon Research & Engineering Company | Synthetic diesel fuel and process for its production |
| US5942197A (en) * | 1996-08-23 | 1999-08-24 | Exxon Research And Engineering Co | Countercurrent reactor |
| US5888376A (en) * | 1996-08-23 | 1999-03-30 | Exxon Research And Engineering Co. | Conversion of fischer-tropsch light oil to jet fuel by countercurrent processing |
| US5906728A (en) * | 1996-08-23 | 1999-05-25 | Exxon Chemical Patents Inc. | Process for increased olefin yields from heavy feedstocks |
| US5766274A (en) | 1997-02-07 | 1998-06-16 | Exxon Research And Engineering Company | Synthetic jet fuel and process for its production |
| US5882505A (en) * | 1997-06-03 | 1999-03-16 | Exxon Research And Engineering Company | Conversion of fisher-tropsch waxes to lubricants by countercurrent processing |
| US5928497A (en) * | 1997-08-22 | 1999-07-27 | Exxon Chemical Pateuts Inc | Heteroatom removal through countercurrent sorption |
| US6495029B1 (en) | 1997-08-22 | 2002-12-17 | Exxon Research And Engineering Company | Countercurrent desulfurization process for refractory organosulfur heterocycles |
| CA2243267C (en) | 1997-09-26 | 2003-12-30 | Exxon Research And Engineering Company | Countercurrent reactor with interstage stripping of nh3 and h2s in gas/liquid contacting zones |
| US6497810B1 (en) | 1998-12-07 | 2002-12-24 | Larry L. Laccino | Countercurrent hydroprocessing with feedstream quench to control temperature |
| US6623621B1 (en) | 1998-12-07 | 2003-09-23 | Exxonmobil Research And Engineering Company | Control of flooding in a countercurrent flow reactor by use of temperature of liquid product stream |
| US6569314B1 (en) | 1998-12-07 | 2003-05-27 | Exxonmobil Research And Engineering Company | Countercurrent hydroprocessing with trickle bed processing of vapor product stream |
| US6579443B1 (en) | 1998-12-07 | 2003-06-17 | Exxonmobil Research And Engineering Company | Countercurrent hydroprocessing with treatment of feedstream to remove particulates and foulant precursors |
| US6835301B1 (en) | 1998-12-08 | 2004-12-28 | Exxon Research And Engineering Company | Production of low sulfur/low aromatics distillates |
| US6514403B1 (en) * | 2000-04-20 | 2003-02-04 | Abb Lummus Global Inc. | Hydrocracking of vacuum gas and other oils using a cocurrent/countercurrent reaction system and a post-treatment reactive distillation system |
| US6617871B2 (en) * | 2001-07-09 | 2003-09-09 | Rambus Inc. | Methods and apparatus for bi-directional signaling |
| US7247235B2 (en) * | 2003-05-30 | 2007-07-24 | Abb Lummus Global Inc, | Hydrogenation of middle distillate using a counter-current reactor |
| ATE458546T1 (de) * | 2003-08-18 | 2010-03-15 | Shell Int Research | Verteilervorrichtung |
| JP4643966B2 (ja) * | 2004-10-01 | 2011-03-02 | Ｊｘ日鉱日石エネルギー株式会社 | 水素化精製軽油の製造方法、水素化精製軽油及び軽油組成物 |
| EP1836284B1 (en) * | 2004-12-23 | 2018-08-22 | The Petroleum Oil and Gas Corporation of South Afr. | Synthetically derived distillate kerosene and its use |
| US20080257783A1 (en) * | 2004-12-23 | 2008-10-23 | The Petroleum Oil And Gas Corporation Of South Africa (Pty) Ltd | Process for Catalytic Conversion of Fischer-Tropsch Derived Olefins to Distillates |
| US8022258B2 (en) | 2005-07-05 | 2011-09-20 | Neste Oil Oyj | Process for the manufacture of diesel range hydrocarbons |
| US12203035B2 (en) | 2005-07-05 | 2025-01-21 | Neste Oyj | Process for the manufacture of diesel range hydrocarbons |
| US8303804B2 (en) * | 2008-10-06 | 2012-11-06 | Exxonmobil Research And Engineering Company | Process to improve jet fuels |
| WO2011061575A1 (en) * | 2009-11-20 | 2011-05-26 | Total Raffinage Marketing | Process for the production of hydrocarbon fluids having a low aromatic content |
| WO2011061576A1 (en) | 2009-11-20 | 2011-05-26 | Total Raffinage Marketing | Process for the production of hydrocarbon fluids having a low aromatic content |
| US9334451B2 (en) * | 2010-03-15 | 2016-05-10 | Saudi Arabian Oil Company | High quality middle distillate production process |
| EP3517591A1 (en) | 2011-02-15 | 2019-07-31 | Neste Oil Oyj | Use of renewable oil in hydrotreatment process |
| FR3015514B1 (fr) | 2013-12-23 | 2016-10-28 | Total Marketing Services | Procede ameliore de desaromatisation de coupes petrolieres |
| CN108291152B (zh) * | 2015-11-23 | 2021-01-08 | 国际壳牌研究有限公司 | 生物质向液态烃物质的转化 |
| BR112018010526B1 (pt) * | 2015-11-23 | 2021-10-05 | Shell Internationale Research Maatschappij B.V. | Processo para produzir produtos de hidrocarboneto líquidos a partir de pelo menos uma dentre uma matéria-prima que contém biomassa e uma matéria-prima derivada de biomassa |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2952626A (en) * | 1957-08-05 | 1960-09-13 | Union Oil Co | Mixed-phase hydrofining of hydrocarbon oils |
| US3147210A (en) * | 1962-03-19 | 1964-09-01 | Union Oil Co | Two stage hydrogenation process |
| GB1141809A (en) * | 1965-10-04 | 1969-02-05 | British Petroleum Co | Improvements relating to the desulphurisation and hydrogenation of aromatic hydrocarbons |
| US3450784A (en) * | 1966-09-22 | 1969-06-17 | Lummus Co | Hydrogenation of benzene to cyclohexane |
| US3513085A (en) * | 1967-09-06 | 1970-05-19 | Arnold M Leas | Producing isoparaffins and naphthenes from hydrocarbons |
| US3573198A (en) * | 1969-02-10 | 1971-03-30 | Universal Oil Prod Co | Smoke point improvement of jet fuel kerosene fractions |
-
1971
- 1971-09-02 US US00177362A patent/US3767562A/en not_active Expired - Lifetime
-
1972
- 1972-08-16 AU AU45635/72A patent/AU469380B2/en not_active Expired
- 1972-08-21 FI FI2312/72A patent/FI59810C/fi active
- 1972-08-25 IT IT5235772A patent/IT962225B/it active
- 1972-08-28 IT IT52397/72A patent/IT962255B/it active
- 1972-08-29 DE DE2242331A patent/DE2242331A1/de not_active Withdrawn
- 1972-08-30 JP JP8705472A patent/JPS5442005B2/ja not_active Expired
- 1972-08-31 FR FR7230998A patent/FR2151059B1/fr not_active Expired
- 1972-08-31 GB GB4048072A patent/GB1399108A/en not_active Expired
- 1972-08-31 CA CA150,651A patent/CA983420A/en not_active Expired
- 1972-09-01 NL NLAANVRAGE7211962,A patent/NL176583C/xx not_active IP Right Cessation
- 1972-09-01 ES ES406277A patent/ES406277A1/es not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| ES406277A1 (es) | 1975-07-01 |
| AU4563572A (en) | 1974-02-21 |
| US3767562A (en) | 1973-10-23 |
| FI59810B (fi) | 1981-06-30 |
| AU469380B2 (en) | 1976-02-12 |
| JPS4834906A (enExample) | 1973-05-23 |
| GB1399108A (en) | 1975-06-25 |
| DE2242331A1 (de) | 1973-03-08 |
| NL176583C (nl) | 1985-05-01 |
| JPS5442005B2 (enExample) | 1979-12-12 |
| FR2151059B1 (enExample) | 1976-08-13 |
| IT962255B (it) | 1973-12-20 |
| CA983420A (en) | 1976-02-10 |
| FR2151059A1 (enExample) | 1973-04-13 |
| NL7211962A (enExample) | 1973-03-06 |
| IT962225B (it) | 1973-12-20 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| FI59810C (fi) | Foerfarande foer framstaellning av braensle foer jetmotor | |
| US5183556A (en) | Production of diesel fuel by hydrogenation of a diesel feed | |
| US9068125B2 (en) | Process for the recovery of pure aromatics from hydrocarbon fractions containing aromatics | |
| FI60228B (fi) | Foerfarande foer framstaellning av jetbraensle | |
| US9580663B2 (en) | Process for hydrocracking a hydrocarbon feedstock | |
| RU2540275C1 (ru) | Способ увеличения производства бензола и толуола | |
| JP4731776B2 (ja) | 炭化水素の改質方法 | |
| US20090050523A1 (en) | Olefin production utilizing whole crude oil/condensate feedstock and selective hydrocracking | |
| US20080277314A1 (en) | Olefin production utilizing whole crude oil/condensate feedstock and hydrotreating | |
| MX2007011038A (es) | Metodo para producir aceite lubricante base a partir de aceite de desecho. | |
| US9315741B2 (en) | Process for ultra low benzene reformate using catalytic distillation | |
| EA030559B1 (ru) | Способ получения ароматических соединений и легких олефинов из углеводородного сырья | |
| JP4208260B2 (ja) | 炭化水素流れにおける芳香族の選択的水素化 | |
| CN101292013B (zh) | 烃残油处理和减粘裂化蒸汽裂化器的原料 | |
| US3846278A (en) | Production of jet fuel | |
| WO1998051648A1 (en) | Process for the alkylation of benzene | |
| EA017890B1 (ru) | Способ снижения содержания серы в углеводородном потоке (варианты) | |
| WO2006088528A2 (en) | Process for the removal of benzene from gasoline streams | |
| FI60229B (fi) | Tillverkning av braensle foer reamotor | |
| RU2291892C1 (ru) | Способ получения бензола | |
| RU2646751C1 (ru) | Способ изомеризации легких бензиновых фракций | |
| SU378024A1 (enExample) | ||
| RU2005767C1 (ru) | Способ переработки прямогонных бензиновых фракций | |
| US1951792A (en) | Process for hydrogenating hydrocarbon oils | |
| RU1838378C (ru) | Способ переработки пр могонных бензиновых фракций |