AR101431A1 - Proceso y aparatos para separar di-olefinas c₅ de naftas de pirólisis - Google Patents
Proceso y aparatos para separar di-olefinas c₅ de naftas de pirólisisInfo
- Publication number
- AR101431A1 AR101431A1 ARP140102173A ARP140102173A AR101431A1 AR 101431 A1 AR101431 A1 AR 101431A1 AR P140102173 A ARP140102173 A AR P140102173A AR P140102173 A ARP140102173 A AR P140102173A AR 101431 A1 AR101431 A1 AR 101431A1
- Authority
- AR
- Argentina
- Prior art keywords
- isoprene
- stream
- hydrocarbon resins
- grade
- producing
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/009—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping in combination with chemical reactions
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/34—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping with one or more auxiliary substances
- B01D3/40—Extractive distillation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/02—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons
- C07C2/50—Diels-Alder conversion
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/005—Processes comprising at least two steps in series
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/04—Purification; Separation; Use of additives by distillation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/04—Purification; Separation; Use of additives by distillation
- C07C7/05—Purification; Separation; Use of additives by distillation with the aid of auxiliary compounds
- C07C7/08—Purification; Separation; Use of additives by distillation with the aid of auxiliary compounds by extractive distillation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/10—Purification; Separation; Use of additives by extraction, i.e. purification or separation of liquid hydrocarbons with the aid of liquids
-
- 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
- C10G7/00—Distillation of hydrocarbon oils
- C10G7/02—Stabilising gasoline by removing gases by fractioning
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2603/00—Systems containing at least three condensed rings
- C07C2603/56—Ring systems containing bridged rings
- C07C2603/58—Ring systems containing bridged rings containing three rings
- C07C2603/60—Ring systems containing bridged rings containing three rings containing at least one ring with less than six members
- C07C2603/66—Ring systems containing bridged rings containing three rings containing at least one ring with less than six members containing five-membered rings
- C07C2603/68—Dicyclopentadienes; Hydrogenated dicyclopentadienes
-
- 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
- C10G2300/1037—Hydrocarbon fractions
- C10G2300/104—Light gasoline having a boiling range of about 20 - 100 °C
-
- 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
- C10G2300/1037—Hydrocarbon fractions
- C10G2300/1044—Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C
-
- 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
- C10G2400/02—Gasoline
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- Water Supply & Treatment (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
Aparatos, sistemas y métodos para producir una corriente de piperilenos para la elaboración de resinas de hidrocarburos C₅ hechas por catálisis que contienen todos los monómeros reactivos clave que ya están presentes en la fracción C₅ de la nafta de pirólisis, que de otra manera se perderían con la corriente de isopreno crudo. Algunas formas de realización de la presente son para producir una corriente de DCPD de grado resina de hidrocarburos que consiste en dímeros y codímeros de isopreno que son valiosos para producir resinas de hidrocarburos térmicas, ya sea isopreno de grado polímero y refinado de calidad nafta (libre de azufre y acetilenos) o una corriente relativamente pequeña de isopreno crudo con un máximo uso del isopreno desplazando parte del isopreno a una corriente de DCPD que se utiliza para fabricar resinas de hidrocarburos térmicas.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201361831447P | 2013-06-05 | 2013-06-05 |
Publications (1)
Publication Number | Publication Date |
---|---|
AR101431A1 true AR101431A1 (es) | 2016-12-21 |
Family
ID=52006001
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ARP140102173A AR101431A1 (es) | 2013-06-05 | 2014-06-03 | Proceso y aparatos para separar di-olefinas c₅ de naftas de pirólisis |
Country Status (8)
Country | Link |
---|---|
US (1) | US10047022B2 (es) |
KR (1) | KR102256614B1 (es) |
CN (2) | CN111454116A (es) |
AR (1) | AR101431A1 (es) |
BR (1) | BR112015030138B8 (es) |
RU (1) | RU2661869C2 (es) |
TW (1) | TWI633086B (es) |
WO (1) | WO2014204670A1 (es) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP6549321B2 (ja) * | 2015-11-04 | 2019-07-24 | エクソンモービル ケミカル パテンツ インコーポレイテッド | シクロペンタジエン及び/又はジシクロペンタジエンを製造する方法及びシステム |
CN108430957A (zh) * | 2015-12-14 | 2018-08-21 | 沙特基础工业全球技术公司 | 由裂解气回收二环戊二烯的方法和系统 |
JP7088161B2 (ja) * | 2017-03-08 | 2022-06-21 | 日本ゼオン株式会社 | 炭化水素の製造方法および製造装置 |
WO2021048657A1 (en) | 2019-09-11 | 2021-03-18 | Sabic Global Technologies B.V. | Recovery of isoprene and cpd from a pygas stream |
Family Cites Families (31)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2436149A (en) * | 1945-12-29 | 1948-02-17 | Standard Oil Dev Co | Extraction of a diolefin |
US2582920A (en) * | 1947-11-07 | 1952-01-15 | Pittsburgh Plate Glass Co | High purity dicyclopentadiene |
US3097249A (en) * | 1960-06-13 | 1963-07-09 | Ici Ltd | Process for separating hydrocarbon mixtures |
US3196188A (en) * | 1961-11-28 | 1965-07-20 | Union Carbide Corp | Cyclopentadiene dimerization process |
GB1093413A (en) * | 1964-11-06 | 1967-11-29 | Internat Synthetic Rubber Comp | Separation of hydrocarbons |
US3510405A (en) * | 1967-11-11 | 1970-05-05 | Nippon Zeon Co | Isoprene purification process |
US3557239A (en) * | 1969-12-31 | 1971-01-19 | Monsanto Co | Treatment of isoprene streams |
AU468106B2 (en) * | 1970-12-29 | 1976-01-08 | Snamprogetti S.P.A. | Process forthe recovery of isophrene from mixtures containing thesame |
BE787944A (fr) * | 1971-08-26 | 1973-02-26 | Shell Int Research | Procede de recuperation d'isoprene |
US4081332A (en) * | 1976-08-27 | 1978-03-28 | The B. F. Goodrich Company | Extractive distillation of C5 hydrocarbons using acetonitrile and additives |
JPS6021125B2 (ja) * | 1976-12-20 | 1985-05-25 | ジェイエスアール株式会社 | イソプレンの精製法 |
JPH0739354B2 (ja) * | 1985-07-08 | 1995-05-01 | 日本ゼオン株式会社 | 高純度ジシクロペンタジエンの製造方法 |
US5401891A (en) * | 1993-12-17 | 1995-03-28 | Exxon Chemical Patents Inc. | Production of polymerization grade dicyclopentadiene |
US6258989B1 (en) * | 1999-09-30 | 2001-07-10 | Phillips Petroleum Company | Hydrocarbon upgrading process |
RU2186051C1 (ru) | 2000-10-30 | 2002-07-27 | Центр по разработке эластомеров Казанского государственного технологического университета | Способ получения дициклопентадиена из c5-фракции пиролиза углеводородов |
CN1162380C (zh) * | 2001-10-12 | 2004-08-18 | 中国石油化工股份有限公司 | 一种裂解碳五馏分的分离方法 |
US6958426B2 (en) * | 2001-09-29 | 2005-10-25 | China Petroleum & Chemical Corporation | Process for separating C5 cuts obtained from a petroleum cracking process |
RU2243960C2 (ru) * | 2002-07-29 | 2005-01-10 | Дядюрин Александр Павлович | Способ разделения фракций углеводородов с5 |
CN100999434A (zh) * | 2006-01-11 | 2007-07-18 | 北京化工大学 | 乙腈溶剂法的碳五馏分分离与综合利用 |
US8066868B1 (en) * | 2006-12-20 | 2011-11-29 | Uop Llc | Fluid catalytic cracking to produce and recover light olefins |
CN101244976B (zh) * | 2007-02-15 | 2011-05-04 | 中国石油化工股份有限公司 | 一种制取聚合级异戊二烯的方法 |
CN101244973B (zh) * | 2007-02-15 | 2010-05-19 | 中国石油化工股份有限公司 | 脱除高纯度异戊二烯中炔烃的方法 |
CN101100412B (zh) * | 2007-07-19 | 2011-03-23 | 中国石油化工集团公司 | 后热二聚分离碳五双烯烃的方法 |
CN100593530C (zh) * | 2007-07-19 | 2010-03-10 | 中国石油化工集团公司 | 石油裂解碳五馏分中双烯烃的分离方法 |
CN101450886A (zh) * | 2007-12-07 | 2009-06-10 | 中国石油化工股份有限公司 | 一种由碳五馏分生产双环戊二烯的方法 |
CN101508621A (zh) * | 2008-02-15 | 2009-08-19 | 中国石油化工股份有限公司 | 分离裂解碳五馏分中二烯烃的方法 |
CN101544533B (zh) * | 2009-05-06 | 2012-11-21 | 南京工业大学 | 用后脱炔烃工艺脱除裂解碳五馏分中的炔烃的方法 |
CN101665400B (zh) * | 2009-09-22 | 2012-05-23 | 宁波金海德旗化工有限公司 | 一种两次蒸出异戊二烯的碳五双烯烃预分离方法 |
US20110178349A1 (en) * | 2010-01-20 | 2011-07-21 | Anzick Robert Kenneth | Method of treating a hydrocarbon stream comprising cyclopentadiene and one or more diolefins |
JP5942986B2 (ja) | 2011-03-31 | 2016-06-29 | 日本ゼオン株式会社 | 炭化水素原料の製造方法 |
CN102516010B (zh) | 2011-11-25 | 2013-10-09 | 大庆华科股份有限公司 | 用于分离石油裂解乙烯副产碳五馏分中的双烯烃组分的方法及设备 |
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2014
- 2014-06-03 AR ARP140102173A patent/AR101431A1/es unknown
- 2014-06-04 TW TW103119403A patent/TWI633086B/zh active
- 2014-06-05 KR KR1020157034785A patent/KR102256614B1/ko active IP Right Grant
- 2014-06-05 US US14/297,412 patent/US10047022B2/en active Active
- 2014-06-05 BR BR112015030138A patent/BR112015030138B8/pt active IP Right Grant
- 2014-06-05 CN CN202010135749.2A patent/CN111454116A/zh active Pending
- 2014-06-05 WO PCT/US2014/041151 patent/WO2014204670A1/en active Application Filing
- 2014-06-05 CN CN201480032356.1A patent/CN105593194A/zh active Pending
- 2014-06-05 RU RU2015153268A patent/RU2661869C2/ru active
Also Published As
Publication number | Publication date |
---|---|
CN111454116A (zh) | 2020-07-28 |
RU2015153268A (ru) | 2017-07-17 |
BR112015030138B8 (pt) | 2022-11-29 |
BR112015030138B1 (pt) | 2021-06-01 |
KR20160015248A (ko) | 2016-02-12 |
KR102256614B1 (ko) | 2021-05-27 |
US10047022B2 (en) | 2018-08-14 |
TWI633086B (zh) | 2018-08-21 |
RU2661869C2 (ru) | 2018-07-20 |
BR112015030138A2 (pt) | 2017-07-25 |
TW201502118A (zh) | 2015-01-16 |
US20140364665A1 (en) | 2014-12-11 |
CN105593194A (zh) | 2016-05-18 |
WO2014204670A1 (en) | 2014-12-24 |
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