BR0109793A - Processo integrado para preparar isoolefinas a partir de gás de sìntese e composição combustìvel destilada - Google Patents
Processo integrado para preparar isoolefinas a partir de gás de sìntese e composição combustìvel destiladaInfo
- Publication number
- BR0109793A BR0109793A BR0109793-8A BR0109793A BR0109793A BR 0109793 A BR0109793 A BR 0109793A BR 0109793 A BR0109793 A BR 0109793A BR 0109793 A BR0109793 A BR 0109793A
- Authority
- BR
- Brazil
- Prior art keywords
- synthesis gas
- fraction
- distilled
- fischer
- tropsch
- Prior art date
Links
- 239000000446 fuel Substances 0.000 title abstract 6
- 230000015572 biosynthetic process Effects 0.000 title abstract 5
- 238000003786 synthesis reaction Methods 0.000 title abstract 5
- 238000004519 manufacturing process Methods 0.000 title 1
- 238000000034 method Methods 0.000 abstract 8
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract 4
- 239000007789 gas Substances 0.000 abstract 3
- 238000006384 oligomerization reaction Methods 0.000 abstract 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract 2
- 239000003345 natural gas Substances 0.000 abstract 2
- 239000001993 wax Substances 0.000 abstract 2
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 abstract 1
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 abstract 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 abstract 1
- 150000001336 alkenes Chemical class 0.000 abstract 1
- 230000008033 biological extinction Effects 0.000 abstract 1
- 239000001257 hydrogen Substances 0.000 abstract 1
- 229910052739 hydrogen Inorganic materials 0.000 abstract 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 abstract 1
- 239000012535 impurity Substances 0.000 abstract 1
- 229910052757 nitrogen Inorganic materials 0.000 abstract 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 abstract 1
- 239000012188 paraffin wax Substances 0.000 abstract 1
- 239000011593 sulfur Substances 0.000 abstract 1
- 229910052717 sulfur Inorganic materials 0.000 abstract 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
- C10G57/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one cracking process or refining process and at least one other conversion process
-
- 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1022—Fischer-Tropsch products
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
"PROCESSO INTEGRADO PARA PREPARAR ISOOLEFINAS A PARTIR DE GáS DE SìNTESE E COMPOSIçãO COMBUSTìVEL DESTILADA". Um processo integrado para produzir combustível destilado a partir de gás de síntese é apresentado. O gás de síntese é reagido sob condições Fischer-Tropsch para formar um fluxo de produto que inclui uma fração de nafta, uma fração de combustível destilado e uma fração que inclui essencialmente cera e produtos pesados. A fração de parafina é submetida ao processo Paragon, e as olefinas leves geradas neste processo são oligomerizadas para formar isoolefinas adicionais, que são opcionalmente reduzidas para formar isoparafinas. Nafta e combustíveis destilados podem é isolados da etapa de oligomerização, e cera e frações pesadas provenientes da etapa de oligomerização são opcionalmente recicladas até a extinção. De preferência, pelo menos uma parte do gás de síntese usado na química de Fischer-Tropsch é derivada de gás natural. Os produtos C~ 3~+ provenientes de gás natural e da etapa Fischer-Tropsch são opcionalmente submetidos aa redistribuição molecular para produzir etano adicional e uma fração C~ 3~+ ou desidrogenados para formar uma alimentação adicional para o processo de oligomerização. Os combustíveis destilados formados neste processo tem valores de octano e/ou cetano relativamente altos e também tem baixos níveis de enxofre e de impurezas de nitrogênio. O processo é vantajoso com respeito a outros processos porque requer significativamente menos hidrogênio, e pode é operado sob temperaturas e pressões consideravelmente mais baixas.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US54211500A | 2000-04-03 | 2000-04-03 | |
PCT/US2001/010393 WO2001074970A2 (en) | 2000-04-03 | 2001-03-30 | Improved conversion of syngas to distillate fuels |
Publications (1)
Publication Number | Publication Date |
---|---|
BR0109793A true BR0109793A (pt) | 2004-02-10 |
Family
ID=24162398
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
BR0109793-8A BR0109793A (pt) | 2000-04-03 | 2001-03-30 | Processo integrado para preparar isoolefinas a partir de gás de sìntese e composição combustìvel destilada |
Country Status (6)
Country | Link |
---|---|
US (1) | US6864398B2 (pt) |
EP (1) | EP1276829A2 (pt) |
JP (1) | JP2004500474A (pt) |
AU (1) | AU2001249695A1 (pt) |
BR (1) | BR0109793A (pt) |
WO (1) | WO2001074970A2 (pt) |
Families Citing this family (29)
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US6441263B1 (en) * | 2000-07-07 | 2002-08-27 | Chevrontexaco Corporation | Ethylene manufacture by use of molecular redistribution on feedstock C3-5 components |
AR036902A1 (es) * | 2001-10-24 | 2004-10-13 | Exxonmobil Chem Patents Inc | Un proceso para la oligomerizacion de un material de alimentacion olefinico, usos de un limite en el nivel de azufre en el material de alimentacion, una mezcla oligomerica olefinica, y un ester o una composicion polimerica plastificada |
WO2003035584A1 (en) * | 2001-10-24 | 2003-05-01 | Exxonmobil Chemical Patents Inc. | Process for the oligomerization of olefins |
JP4748939B2 (ja) * | 2002-01-31 | 2011-08-17 | シェブロン ユー.エス.エー. インコーポレイテッド | フィッシャー・トロプシュおよび石油由来のナフサおよび留出物のアップグレード化 |
US6713657B2 (en) * | 2002-04-04 | 2004-03-30 | Chevron U.S.A. Inc. | Condensation of olefins in fischer tropsch tail gas |
JP2005533158A (ja) * | 2002-07-19 | 2005-11-04 | シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ | 液体炭化水素の燃焼方法 |
WO2004009743A1 (en) * | 2002-07-19 | 2004-01-29 | Shell Internationale Research Maatschappij B.V. | Use of a yellow flame burner |
CA2493884A1 (en) * | 2002-07-19 | 2004-01-29 | Shell Internationale Research Maatschappij B.V. | Use of a blue flame burner |
NL1026215C2 (nl) * | 2003-05-19 | 2005-07-08 | Sasol Tech Pty Ltd | Koolwaterstofsamenstelling voor gebruik in CI motoren. |
US7678952B2 (en) * | 2003-05-27 | 2010-03-16 | Shell Oil Company | Process to prepare a gasoline |
RU2006146061A (ru) * | 2004-05-26 | 2008-07-10 | Шелл Интернэшнл Рисерч Маатсхаппий Б.В. (NL) | Алифатический компонент бензина и способ его получения |
BRPI0510476A (pt) * | 2004-05-26 | 2007-11-06 | Shell Int Research | processo para preparar um gasóleo |
FR2871167B1 (fr) * | 2004-06-04 | 2006-08-04 | Inst Francais Du Petrole | Procede d'amelioration de coupes essences et de transformation en gazoles |
US20080142410A1 (en) * | 2004-12-30 | 2008-06-19 | Cruijsberg Emil Eduard Antoniu | Process for the Preparation of Lower Olefins from Heavy Wax |
CN101253132A (zh) * | 2005-07-08 | 2008-08-27 | 北卡罗来纳-查佩尔山大学 | 用于烷烃易位的双催化剂体系 |
FR2888584B1 (fr) * | 2005-07-18 | 2010-12-10 | Inst Francais Du Petrole | Procede de production de distillats moyens par hydroisomerisation et hydrocraquage de charges issues du procede fischer-tropsch utilisant un lit de garde multifonctionnel |
DE102005035988B4 (de) * | 2005-07-28 | 2009-01-02 | Wolf, Bodo Max, Dr.-Ing. | Verfahren zur Erzeugung von flüssigen Kohlenwasserstoffen aus Gas |
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US8624069B2 (en) * | 2008-08-08 | 2014-01-07 | Afognak Native Corporation | Conversion of biomass feedstocks into hydrocarbon liquid transportation fuels |
TWI462777B (zh) * | 2009-10-30 | 2014-12-01 | Atomic Energy Council | 合成甲醇及二甲醚之Cu-Zn-Al觸媒製備方法 |
FR2952380B1 (fr) * | 2009-11-10 | 2012-05-18 | Inst Francais Du Petrole | Procede de production de distillat moyen a partir de cires fischer tropsch mettant en oeuvre un catalyseur a base de zeolithe modifiee par un traitement basique |
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US20140206915A1 (en) * | 2013-01-18 | 2014-07-24 | Chevron U.S.A. Inc. | Paraffinic jet and diesel fuels and base oils from vegetable oils via a combination of hydrotreating, paraffin disproportionation and hydroisomerization |
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RU2634445C1 (ru) * | 2016-07-01 | 2017-10-30 | Федеральное государственное унитарное предприятие "Крыловский государственный научный центр" | Технологический комплекс получения синтез-газа в установке по переработке попутного нефтяного газа в синтетическую нефть на гравитационной платформе gtl |
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-
2001
- 2001-03-30 AU AU2001249695A patent/AU2001249695A1/en not_active Abandoned
- 2001-03-30 WO PCT/US2001/010393 patent/WO2001074970A2/en not_active Application Discontinuation
- 2001-03-30 EP EP01922948A patent/EP1276829A2/en not_active Withdrawn
- 2001-03-30 BR BR0109793-8A patent/BR0109793A/pt not_active Application Discontinuation
- 2001-03-30 JP JP2001572647A patent/JP2004500474A/ja active Pending
- 2001-12-28 US US10/034,241 patent/US6864398B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
EP1276829A2 (en) | 2003-01-22 |
JP2004500474A (ja) | 2004-01-08 |
US20020111521A1 (en) | 2002-08-15 |
AU2001249695A1 (en) | 2001-10-15 |
WO2001074970A2 (en) | 2001-10-11 |
WO2001074970A3 (en) | 2002-05-30 |
US6864398B2 (en) | 2005-03-08 |
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