NO330272B1 - Fremgangsmate for hydrogenbehandling av hydrokarbonrastoff - Google Patents
Fremgangsmate for hydrogenbehandling av hydrokarbonrastoff Download PDFInfo
- Publication number
- NO330272B1 NO330272B1 NO20021004A NO20021004A NO330272B1 NO 330272 B1 NO330272 B1 NO 330272B1 NO 20021004 A NO20021004 A NO 20021004A NO 20021004 A NO20021004 A NO 20021004A NO 330272 B1 NO330272 B1 NO 330272B1
- Authority
- NO
- Norway
- Prior art keywords
- hydrogen
- hydrocarbon
- reactor
- gas
- zone
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims description 149
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims description 101
- 239000001257 hydrogen Substances 0.000 title claims description 98
- 229910052739 hydrogen Inorganic materials 0.000 title claims description 98
- 229930195733 hydrocarbon Natural products 0.000 title claims description 77
- 150000002430 hydrocarbons Chemical class 0.000 title claims description 77
- 239000004215 Carbon black (E152) Substances 0.000 title claims description 76
- 230000008569 process Effects 0.000 title description 86
- 239000007789 gas Substances 0.000 claims description 85
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 60
- 229910052717 sulfur Inorganic materials 0.000 claims description 55
- 239000011593 sulfur Substances 0.000 claims description 55
- 239000012071 phase Substances 0.000 claims description 38
- 239000003054 catalyst Substances 0.000 claims description 29
- 239000002994 raw material Substances 0.000 claims description 28
- 239000000047 product Substances 0.000 claims description 27
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 claims description 20
- 238000011144 upstream manufacturing Methods 0.000 claims description 14
- 239000013067 intermediate product Substances 0.000 claims description 7
- 150000002431 hydrogen Chemical class 0.000 claims description 6
- 239000012467 final product Substances 0.000 claims description 5
- 229910000037 hydrogen sulfide Inorganic materials 0.000 claims description 4
- 239000007791 liquid phase Substances 0.000 claims description 4
- 239000012535 impurity Substances 0.000 claims 1
- 238000002474 experimental method Methods 0.000 description 28
- 150000003464 sulfur compounds Chemical class 0.000 description 12
- 238000006243 chemical reaction Methods 0.000 description 10
- 239000007788 liquid Substances 0.000 description 10
- 239000005864 Sulphur Substances 0.000 description 6
- 230000008901 benefit Effects 0.000 description 6
- 238000006477 desulfuration reaction Methods 0.000 description 5
- 230000023556 desulfurization Effects 0.000 description 5
- 239000000446 fuel Substances 0.000 description 5
- 239000007795 chemical reaction product Substances 0.000 description 4
- 239000003344 environmental pollutant Substances 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- 238000011835 investigation Methods 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 238000013461 design Methods 0.000 description 2
- 230000002349 favourable effect Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- KAPUZOVRULFWAA-UHFFFAOYSA-N 1-butylphenanthrene Chemical compound C1=CC2=CC=CC=C2C2=C1C(CCCC)=CC=C2 KAPUZOVRULFWAA-UHFFFAOYSA-N 0.000 description 1
- XOETUHBIDWDVSF-UHFFFAOYSA-N 1-heptyl-2-phenylbenzene Chemical group CCCCCCCC1=CC=CC=C1C1=CC=CC=C1 XOETUHBIDWDVSF-UHFFFAOYSA-N 0.000 description 1
- LCOFDOQQJQFUQF-UHFFFAOYSA-N 1-heptyldibenzothiophene Chemical group S1C2=CC=CC=C2C2=C1C=CC=C2CCCCCCC LCOFDOQQJQFUQF-UHFFFAOYSA-N 0.000 description 1
- ZARGURXLAHEGDJ-UHFFFAOYSA-N CCCC[S+](C=C1)C(C=C2)=C1C1=C2C(C=CC=C2)=C2C=C1 Chemical compound CCCC[S+](C=C1)C(C=C2)=C1C1=C2C(C=CC=C2)=C2C=C1 ZARGURXLAHEGDJ-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 230000001066 destructive effect Effects 0.000 description 1
- -1 diesel Substances 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 230000002085 persistent effect Effects 0.000 description 1
- 238000005504 petroleum refining Methods 0.000 description 1
- 150000003463 sulfur Chemical class 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
- C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
- C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
- C10G65/04—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps
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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Separation By Low-Temperature Treatments (AREA)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/797,448 US6649042B2 (en) | 2001-03-01 | 2001-03-01 | Hydroprocessing process |
Publications (3)
Publication Number | Publication Date |
---|---|
NO20021004D0 NO20021004D0 (no) | 2002-02-28 |
NO20021004L NO20021004L (no) | 2002-09-02 |
NO330272B1 true NO330272B1 (no) | 2011-03-14 |
Family
ID=25170860
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
NO20021004A NO330272B1 (no) | 2001-03-01 | 2002-02-28 | Fremgangsmate for hydrogenbehandling av hydrokarbonrastoff |
Country Status (9)
Country | Link |
---|---|
US (2) | US6649042B2 (pt) |
EP (1) | EP1236788B1 (pt) |
AR (1) | AR032934A1 (pt) |
AT (1) | ATE362969T1 (pt) |
BR (1) | BR0200574B8 (pt) |
DE (1) | DE60220201T2 (pt) |
ES (1) | ES2287197T3 (pt) |
MX (1) | MX227439B (pt) |
NO (1) | NO330272B1 (pt) |
Families Citing this family (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7166209B2 (en) | 2001-03-01 | 2007-01-23 | Intevep, S.A. | Hydroprocessing process |
US6656348B2 (en) | 2001-03-01 | 2003-12-02 | Intevep, S.A. | Hydroprocessing process |
TWI296651B (en) * | 2003-06-10 | 2008-05-11 | Hydrotreating process | |
US7906013B2 (en) | 2006-12-29 | 2011-03-15 | Uop Llc | Hydrocarbon conversion process |
US7794585B2 (en) * | 2007-10-15 | 2010-09-14 | Uop Llc | Hydrocarbon conversion process |
US9279087B2 (en) * | 2008-06-30 | 2016-03-08 | Uop Llc | Multi-staged hydroprocessing process and system |
US8999141B2 (en) * | 2008-06-30 | 2015-04-07 | Uop Llc | Three-phase hydroprocessing without a recycle gas compressor |
US8008534B2 (en) * | 2008-06-30 | 2011-08-30 | Uop Llc | Liquid phase hydroprocessing with temperature management |
US8221706B2 (en) * | 2009-06-30 | 2012-07-17 | Uop Llc | Apparatus for multi-staged hydroprocessing |
US8518241B2 (en) * | 2009-06-30 | 2013-08-27 | Uop Llc | Method for multi-staged hydroprocessing |
CA2937478C (en) * | 2014-02-10 | 2021-03-09 | Archer Daniels Midland Company | Improved multiphase low mixing processes |
US11788017B2 (en) | 2017-02-12 | 2023-10-17 | Magëmã Technology LLC | Multi-stage process and device for reducing environmental contaminants in heavy marine fuel oil |
US12025435B2 (en) | 2017-02-12 | 2024-07-02 | Magēmã Technology LLC | Multi-stage device and process for production of a low sulfur heavy marine fuel oil |
US10604709B2 (en) | 2017-02-12 | 2020-03-31 | Magēmā Technology LLC | Multi-stage device and process for production of a low sulfur heavy marine fuel oil from distressed heavy fuel oil materials |
US12071592B2 (en) | 2017-02-12 | 2024-08-27 | Magēmā Technology LLC | Multi-stage process and device utilizing structured catalyst beds and reactive distillation for the production of a low sulfur heavy marine fuel oil |
US10655074B2 (en) | 2017-02-12 | 2020-05-19 | Mag{hacek over (e)}m{hacek over (a)} Technology LLC | Multi-stage process and device for reducing environmental contaminates in heavy marine fuel oil |
Family Cites Families (27)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3691152A (en) * | 1971-03-10 | 1972-09-12 | Texaco Inc | Hydrodesulfurization and blending of residue-containing petroleum oil |
US3809664A (en) | 1973-08-16 | 1974-05-07 | Us Agriculture | Method of preparing starch graft polymers |
US4431525A (en) | 1982-04-26 | 1984-02-14 | Standard Oil Company (Indiana) | Three-catalyst process for the hydrotreating of heavy hydrocarbon streams |
US4877647A (en) | 1986-04-17 | 1989-10-31 | Kansas State University Research Foundation | Method of coating substrates with solvated clusters of metal particles |
GB8910711D0 (en) | 1989-05-10 | 1989-06-28 | Davy Mckee London | Process |
US5110444A (en) | 1990-08-03 | 1992-05-05 | Uop | Multi-stage hydrodesulfurization and hydrogenation process for distillate hydrocarbons |
US5183556A (en) | 1991-03-13 | 1993-02-02 | Abb Lummus Crest Inc. | Production of diesel fuel by hydrogenation of a diesel feed |
US5779992A (en) | 1993-08-18 | 1998-07-14 | Catalysts & Chemicals Industries Co., Ltd. | Process for hydrotreating heavy oil and hydrotreating apparatus |
US5759939A (en) | 1994-04-08 | 1998-06-02 | Kansas State University Research Foundation | Composite metal oxide adsorbents |
EP0793701B1 (en) | 1994-11-25 | 1999-01-27 | Kvaerner Process Technology Limited | Multi-step hydrodesulfurization process |
US5935420A (en) | 1996-08-23 | 1999-08-10 | Exxon Research And Engineering Co. | Desulfurization process for refractory organosulfur heterocycles |
US5985131A (en) | 1996-08-23 | 1999-11-16 | Exxon Research And Engineering Company | Hydroprocessing in a countercurrent reaction vessel |
US5939031A (en) | 1996-08-23 | 1999-08-17 | Exxon Research And Engineering Co. | Countercurrent reactor |
US5928498A (en) | 1996-08-23 | 1999-07-27 | Exxon Research And Engineering Co. | Desulfurization and ring opening of petroleum streams |
US6007787A (en) | 1996-08-23 | 1999-12-28 | Exxon Research And Engineering Co. | Countercurrent reaction vessel |
US5925239A (en) | 1996-08-23 | 1999-07-20 | Exxon Research And Engineering Co. | Desulfurization and aromatic saturation of feedstreams containing refractory organosulfur heterocycles and aromatics |
US5705052A (en) | 1996-12-31 | 1998-01-06 | Exxon Research And Engineering Company | Multi-stage hydroprocessing in a single reaction vessel |
US5720872A (en) | 1996-12-31 | 1998-02-24 | Exxon Research And Engineering Company | Multi-stage hydroprocessing with multi-stage stripping in a single stripper vessel |
US6017442A (en) | 1997-09-18 | 2000-01-25 | Phillips Petroleum Company | Hydrocarbon conversion with dual metal promoted zeolite |
US6017443A (en) * | 1998-02-05 | 2000-01-25 | Mobil Oil Corporation | Hydroprocessing process having staged reaction zones |
US6054041A (en) | 1998-05-06 | 2000-04-25 | Exxon Research And Engineering Co. | Three stage cocurrent liquid and vapor hydroprocessing |
US6036844A (en) * | 1998-05-06 | 2000-03-14 | Exxon Research And Engineering Co. | Three stage hydroprocessing including a vapor stage |
US5985136A (en) | 1998-06-18 | 1999-11-16 | Exxon Research And Engineering Co. | Two stage hydrodesulfurization process |
US6087294A (en) | 1998-08-12 | 2000-07-11 | Kansas State University Research Foundation | Dispersion and stabilization of reactive atoms on the surface of metal oxides |
US5968346A (en) | 1998-09-16 | 1999-10-19 | Exxon Research And Engineering Co. | Two stage hydroprocessing with vapor-liquid interstage contacting for vapor heteroatom removal |
US5985135A (en) * | 1998-10-23 | 1999-11-16 | Exxon Research And Engineering Co. | Staged upflow and downflow hydroprocessing with noncatalytic removal of upflow stage vapor impurities |
US6632350B2 (en) * | 2000-10-10 | 2003-10-14 | Exxonmobile Research And Engineering Company | Two stage hydroprocessing and stripping in a single reaction vessel |
-
2001
- 2001-03-01 US US09/797,448 patent/US6649042B2/en not_active Expired - Lifetime
-
2002
- 2002-02-27 ES ES02004489T patent/ES2287197T3/es not_active Expired - Lifetime
- 2002-02-27 EP EP02004489A patent/EP1236788B1/en not_active Expired - Lifetime
- 2002-02-27 AT AT02004489T patent/ATE362969T1/de not_active IP Right Cessation
- 2002-02-27 DE DE60220201T patent/DE60220201T2/de not_active Expired - Lifetime
- 2002-02-28 MX MXPA02002187 patent/MX227439B/es active IP Right Grant
- 2002-02-28 NO NO20021004A patent/NO330272B1/no not_active IP Right Cessation
- 2002-03-01 AR ARP020100759A patent/AR032934A1/es active IP Right Grant
- 2002-03-01 BR BRPI0200574-3B8A patent/BR0200574B8/pt not_active IP Right Cessation
- 2002-05-23 US US10/155,589 patent/US7097815B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
NO20021004L (no) | 2002-09-02 |
ES2287197T3 (es) | 2007-12-16 |
ATE362969T1 (de) | 2007-06-15 |
AR032934A1 (es) | 2003-12-03 |
EP1236788A2 (en) | 2002-09-04 |
DE60220201T2 (de) | 2008-01-17 |
DE60220201D1 (de) | 2007-07-05 |
US7097815B2 (en) | 2006-08-29 |
BR0200574A (pt) | 2002-12-10 |
BR0200574B1 (pt) | 2014-04-01 |
US6649042B2 (en) | 2003-11-18 |
EP1236788A3 (en) | 2003-01-15 |
NO20021004D0 (no) | 2002-02-28 |
BR0200574B8 (pt) | 2014-06-03 |
MXPA02002187A (es) | 2002-09-30 |
EP1236788B1 (en) | 2007-05-23 |
US20030047491A1 (en) | 2003-03-13 |
MX227439B (es) | 2005-04-25 |
US20020162772A1 (en) | 2002-11-07 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
MM1K | Lapsed by not paying the annual fees |