ZA200403513B - Process for maximizing 371° + production in a Fischer-Tropsch process. - Google Patents
Process for maximizing 371° + production in a Fischer-Tropsch process. Download PDFInfo
- Publication number
- ZA200403513B ZA200403513B ZA200403513A ZA200403513A ZA200403513B ZA 200403513 B ZA200403513 B ZA 200403513B ZA 200403513 A ZA200403513 A ZA 200403513A ZA 200403513 A ZA200403513 A ZA 200403513A ZA 200403513 B ZA200403513 B ZA 200403513B
- Authority
- ZA
- South Africa
- Prior art keywords
- catalyst
- conversion
- reactor
- initial
- synthesis gas
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims description 57
- 230000008569 process Effects 0.000 title claims description 54
- 238000004519 manufacturing process Methods 0.000 title description 18
- 239000003054 catalyst Substances 0.000 claims description 66
- 238000006243 chemical reaction Methods 0.000 claims description 61
- 229930195733 hydrocarbon Natural products 0.000 claims description 42
- 150000002430 hydrocarbons Chemical class 0.000 claims description 42
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 42
- 238000003786 synthesis reaction Methods 0.000 claims description 40
- 230000015572 biosynthetic process Effects 0.000 claims description 38
- 239000004215 Carbon black (E152) Substances 0.000 claims description 32
- 239000007789 gas Substances 0.000 claims description 31
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 23
- 239000007788 liquid Substances 0.000 claims description 21
- 239000002002 slurry Substances 0.000 claims description 13
- 230000000694 effects Effects 0.000 claims description 12
- 230000003247 decreasing effect Effects 0.000 claims description 9
- 229910052739 hydrogen Inorganic materials 0.000 claims description 9
- 239000001257 hydrogen Substances 0.000 claims description 8
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 6
- 229910017052 cobalt Inorganic materials 0.000 claims description 4
- 239000010941 cobalt Substances 0.000 claims description 4
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 4
- 239000000047 product Substances 0.000 description 28
- 238000009835 boiling Methods 0.000 description 13
- 230000009849 deactivation Effects 0.000 description 10
- 229910052751 metal Inorganic materials 0.000 description 10
- 239000002184 metal Substances 0.000 description 10
- 239000001993 wax Substances 0.000 description 7
- 239000000463 material Substances 0.000 description 6
- 150000002739 metals Chemical class 0.000 description 6
- OFPXSFXSNFPTHF-UHFFFAOYSA-N oxaprozin Chemical compound O1C(CCC(=O)O)=NC(C=2C=CC=CC=2)=C1C1=CC=CC=C1 OFPXSFXSNFPTHF-UHFFFAOYSA-N 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000012071 phase Substances 0.000 description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 3
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 3
- 229910052717 sulfur Inorganic materials 0.000 description 3
- 239000011593 sulfur Substances 0.000 description 3
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 229910052735 hafnium Inorganic materials 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000012263 liquid product Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000011020 pilot scale process Methods 0.000 description 2
- 229910052697 platinum Inorganic materials 0.000 description 2
- 229910052702 rhenium Inorganic materials 0.000 description 2
- 229910052707 ruthenium Inorganic materials 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 238000012935 Averaging Methods 0.000 description 1
- 235000009581 Balanites aegyptiaca Nutrition 0.000 description 1
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000003190 augmentative effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000004517 catalytic hydrocracking Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- -1 cobalt and iron Chemical class 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 230000002939 deleterious effect Effects 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 150000002009 diols Chemical class 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- VBJZVLUMGGDVMO-UHFFFAOYSA-N hafnium atom Chemical compound [Hf] VBJZVLUMGGDVMO-UHFFFAOYSA-N 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 229910052741 iridium Inorganic materials 0.000 description 1
- GKOZUEZYRPOHIO-UHFFFAOYSA-N iridium atom Chemical compound [Ir] GKOZUEZYRPOHIO-UHFFFAOYSA-N 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000002923 metal particle Substances 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 231100000572 poisoning Toxicity 0.000 description 1
- 230000000607 poisoning effect Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 230000003716 rejuvenation Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- WUAPFZMCVAUBPE-UHFFFAOYSA-N rhenium atom Chemical compound [Re] WUAPFZMCVAUBPE-UHFFFAOYSA-N 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000010454 slate Substances 0.000 description 1
- 239000011949 solid catalyst Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
- 238000011282 treatment Methods 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
Classifications
-
- 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
- C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
- C10G2/30—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
- C10G2/32—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
-
- 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
- C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
- C10G2/30—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
- C10G2/32—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
- C10G2/33—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts characterised by the catalyst used
- C10G2/331—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts characterised by the catalyst used containing group VIII-metals
- C10G2/332—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts characterised by the catalyst used containing group VIII-metals of the iron-group
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US09/996,416 US6458857B1 (en) | 2001-11-20 | 2001-11-20 | Process for maximizing 371° C.+ production in fischer-tropsch process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ZA200403513B true ZA200403513B (en) | 2005-05-23 |
Family
ID=25542890
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ZA200403513A ZA200403513B (en) | 2001-11-20 | 2004-05-07 | Process for maximizing 371° + production in a Fischer-Tropsch process. |
Country Status (13)
| Country | Link |
|---|---|
| US (1) | US6458857B1 (de) |
| EP (1) | EP1448748B1 (de) |
| JP (1) | JP4225910B2 (de) |
| CN (1) | CN1267527C (de) |
| AR (1) | AR037052A1 (de) |
| AT (1) | ATE362968T1 (de) |
| AU (1) | AU2002340136B2 (de) |
| CA (1) | CA2467520C (de) |
| DE (1) | DE60220308T2 (de) |
| ES (1) | ES2286295T3 (de) |
| SA (1) | SA02230403B1 (de) |
| WO (1) | WO2003044128A2 (de) |
| ZA (1) | ZA200403513B (de) |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20050154069A1 (en) * | 2004-01-13 | 2005-07-14 | Syntroleum Corporation | Fischer-Tropsch process in the presence of nitrogen contaminants |
| US7022742B2 (en) * | 2004-04-08 | 2006-04-04 | Syntroleum Corporation | Process to control nitrogen-containing compounds in synthesis gas |
| WO2006099573A1 (en) | 2005-03-16 | 2006-09-21 | Fuelcor Llc | Systems, methods, and compositions for production of synthetic hydrocarbon compounds |
| KR100998083B1 (ko) * | 2008-09-25 | 2010-12-16 | 한국화학연구원 | 피셔―트롭쉬 합성용 슬러리 반응에 의한 액체 탄화수소 화합물의 제조방법 |
| CN103221513B (zh) * | 2010-10-27 | 2015-06-03 | 沙索技术有限公司 | 采用随时间失活的催化剂的工艺操作 |
| PE20171029A1 (es) | 2014-11-20 | 2017-07-17 | Sasol Tech Pty Ltd | Sintesis de fischer-tropsch |
| WO2017037169A1 (en) * | 2015-09-04 | 2017-03-09 | Shell Internationale Research Maatschappij B.V. | Fischer-tropsch process |
| CN105148805B (zh) * | 2015-10-15 | 2017-07-28 | 中国科学院山西煤炭化学研究所 | 一种适用于费托合成介质循环工艺的反应器及应用 |
| CN105219420B (zh) * | 2015-10-20 | 2016-12-07 | 天津大学 | 一种用生物质全组分制备车用生物燃油的装置 |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2271259A (en) * | 1937-01-20 | 1942-01-27 | American Lurgi Corp | Process for synthesizing hydrocarbons |
| US2479999A (en) * | 1945-05-28 | 1949-08-23 | Phillips Petroleum Co | Regeneration of catalysts used in the production of hydrocarbons from carbon monoxide and hydrogen |
| US2610200A (en) * | 1946-05-15 | 1952-09-09 | Phillips Petroleum Co | Synthesis of hydrocarbons |
| GB676635A (en) * | 1949-06-09 | 1952-07-30 | Hydrocarbon Research Inc | Improvements in or relating to hydrocarbon synthesis |
| US5545674A (en) * | 1987-05-07 | 1996-08-13 | Exxon Research And Engineering Company | Surface supported cobalt catalysts, process utilizing these catalysts for the preparation of hydrocarbons from synthesis gas and process for the preparation of said catalysts |
| US5140050A (en) * | 1988-11-23 | 1992-08-18 | Exxon Research And Engineering Co. | Titania catalysts, their preparation, and use in Fischer-Tropsch synthesis |
| US6284807B1 (en) * | 1995-08-08 | 2001-09-04 | Exxon Research And Engineering Company | Slurry hydrocarbon synthesis process with increased catalyst life |
-
2001
- 2001-11-20 US US09/996,416 patent/US6458857B1/en not_active Expired - Fee Related
-
2002
- 2002-10-08 EP EP02778479A patent/EP1448748B1/de not_active Expired - Lifetime
- 2002-10-08 AU AU2002340136A patent/AU2002340136B2/en not_active Ceased
- 2002-10-08 ES ES02778479T patent/ES2286295T3/es not_active Expired - Lifetime
- 2002-10-08 DE DE60220308T patent/DE60220308T2/de not_active Expired - Lifetime
- 2002-10-08 CN CN02822999.1A patent/CN1267527C/zh not_active Expired - Fee Related
- 2002-10-08 WO PCT/US2002/032190 patent/WO2003044128A2/en active IP Right Grant
- 2002-10-08 CA CA2467520A patent/CA2467520C/en not_active Expired - Fee Related
- 2002-10-08 JP JP2003545754A patent/JP4225910B2/ja not_active Expired - Fee Related
- 2002-10-08 AT AT02778479T patent/ATE362968T1/de not_active IP Right Cessation
- 2002-10-27 SA SA02230403A patent/SA02230403B1/ar unknown
- 2002-10-28 AR ARP020104086A patent/AR037052A1/es unknown
-
2004
- 2004-05-07 ZA ZA200403513A patent/ZA200403513B/en unknown
Also Published As
| Publication number | Publication date |
|---|---|
| DE60220308T2 (de) | 2008-01-24 |
| AU2002340136B2 (en) | 2007-09-06 |
| EP1448748B1 (de) | 2007-05-23 |
| CN1267527C (zh) | 2006-08-02 |
| JP2005509726A (ja) | 2005-04-14 |
| EP1448748A2 (de) | 2004-08-25 |
| JP4225910B2 (ja) | 2009-02-18 |
| US6458857B1 (en) | 2002-10-01 |
| ES2286295T3 (es) | 2007-12-01 |
| ATE362968T1 (de) | 2007-06-15 |
| WO2003044128A3 (en) | 2004-02-12 |
| CA2467520C (en) | 2011-05-17 |
| AU2002340136A1 (en) | 2003-06-10 |
| AR037052A1 (es) | 2004-10-20 |
| CN1589309A (zh) | 2005-03-02 |
| CA2467520A1 (en) | 2003-05-30 |
| SA02230403B1 (ar) | 2007-04-24 |
| WO2003044128A2 (en) | 2003-05-30 |
| DE60220308D1 (de) | 2007-07-05 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| RU2101324C1 (ru) | Способ получения углеводородного топлива | |
| US6765026B2 (en) | Process for carbon monoxide hydrogenation | |
| US5958985A (en) | Process for the preparation of hydrocarbons | |
| EP1220715B1 (de) | Verfahren zur wiederbelebung von mit schwefel verunreinigten kobalt-titaniakatalysatoren | |
| JP2009513729A (ja) | フィッシャー・トロプシュ生成物の製造方法 | |
| EP1819438A1 (de) | Promotierte fischer-tropsch-katalysatoren | |
| US20030150777A1 (en) | Process for upgrading Fischer-Tropsch products using dewaxing and hydrofinishing | |
| ZA200403513B (en) | Process for maximizing 371° + production in a Fischer-Tropsch process. | |
| US20020151605A1 (en) | Increased liquid sensitivity during Fischer-Tropsch synthesis by olefin incorporation | |
| AU2003229055B2 (en) | Process for upgrading fischer-tropsch products using dewaxing and hydrofinishing | |
| CA2387027A1 (en) | Process for the preparation of high activity carbon monoxide hydrogenation catalyst and the catalyst composition obtained | |
| JP4261200B2 (ja) | フィッシャー−トロプシュ生成物および原油画分の共水素精製 | |
| Wittenbrink et al. | Process for maximizing 371 C. &plus production in fischer-tropsch process | |
| US20230141033A1 (en) | Selective production of n-paraffin hydrocracking products from heavier n-paraffins | |
| AU2005267518A1 (en) | Integrated plant process to produce high molecular weight basestocks from Fischer-Tropsch wax | |
| WO2022047282A1 (en) | Process and system for base oil production | |
| ZA200509230B (en) | Process for upgrading fischer-tropsch products using dewaxing and hydrofinishing |