GB1420796A - Separation of aromatic isomers - Google Patents
Separation of aromatic isomersInfo
- Publication number
- GB1420796A GB1420796A GB5361273A GB5361273A GB1420796A GB 1420796 A GB1420796 A GB 1420796A GB 5361273 A GB5361273 A GB 5361273A GB 5361273 A GB5361273 A GB 5361273A GB 1420796 A GB1420796 A GB 1420796A
- Authority
- GB
- United Kingdom
- Prior art keywords
- stream
- adsorption
- xylene
- ethylbenzene
- desorption
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- 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
-
- 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
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
- B01J20/16—Alumino-silicates
- B01J20/18—Synthetic zeolitic molecular sieves
- B01J20/186—Chemical treatments in view of modifying the properties of the sieve, e.g. increasing the stability or the activity, also decreasing the activity
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/20—Silicates
- C01B33/26—Aluminium-containing silicates, i.e. silico-aluminates
- C01B33/28—Base exchange silicates, e.g. zeolites
- C01B33/2807—Zeolitic silicoaluminates with a tridimensional crystalline structure possessing molecular sieve properties; Isomorphous compounds wherein a part of the aluminium ore of the silicon present may be replaced by other elements such as gallium, germanium, phosphorus; Preparation of zeolitic molecular sieves from molecular sieves of another type or from preformed reacting mixtures
- C01B33/2876—Zeolitic silicoaluminates with a tridimensional crystalline structure possessing molecular sieve properties; Isomorphous compounds wherein a part of the aluminium ore of the silicon present may be replaced by other elements such as gallium, germanium, phosphorus; Preparation of zeolitic molecular sieves from molecular sieves of another type or from preformed reacting mixtures from a reacting mixture containing an amine or an organic cation, e.g. a quaternary onium cation-ammonium, phosphonium, stibonium
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/12—Purification; Separation; Use of additives by adsorption, i.e. purification or separation of hydrocarbons with the aid of solids, e.g. with ion-exchangers
- C07C7/13—Purification; Separation; Use of additives by adsorption, i.e. purification or separation of hydrocarbons with the aid of solids, e.g. with ion-exchangers by molecular-sieve technique
Abstract
1420796 Separating C 8 aromatic isomers by adsorption MOBIL OIL CORP 19 Nov 1973 [28 Nov 1972] 53612/73 Heading C5E A C 8 aromatic mixture is separated into a first stream comprising meta and ortho xylenes and a second stream comprising para xylene and ethylbenzene by selective adsorption of the latter stream on a ZSM.5 or ZSM.8 zeolite which is disposed in at least two parallel columns which are operated such that adsorption is carried out in one column while desorption is effected in the other and vice versa, m and o xylenes being recovered during the adsorption stages and p-xylene and ethylbenzene during the desorption stages. The meta and ortho xylene stream may be distilled to recover the components, the latter being isomerized and recycled to the adsorption. The isomerization may be carried out at 250-1000‹ F. with a zeolite catalyst and in the presence of toluene as diluent. The second stream may be subjected to crystallization to recover p-xylene and ethylbenzene. Desorption may be effected by (1) reduction in the partial pressure of the sorbed materials in the vapour phase surrounding the adsorbent, (2) lowering the total pressure of the system, (3) heating the adsorbent or preferably (4) purging with an inert desorbent gas or vapour, e.g. steam, He, N 2 , toluene or benzene.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US31005472A | 1972-11-28 | 1972-11-28 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1420796A true GB1420796A (en) | 1976-01-14 |
Family
ID=23200805
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB5361273A Expired GB1420796A (en) | 1972-11-28 | 1973-11-19 | Separation of aromatic isomers |
Country Status (8)
Country | Link |
---|---|
JP (1) | JPS5046631A (en) |
AU (1) | AU6246673A (en) |
BE (1) | BE807878A (en) |
CA (1) | CA1059928A (en) |
DE (1) | DE2359378A1 (en) |
GB (1) | GB1420796A (en) |
IT (1) | IT1001436B (en) |
NL (1) | NL7316302A (en) |
Cited By (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0003622A1 (en) * | 1978-02-07 | 1979-08-22 | Shell Internationale Researchmaatschappij B.V. | Process for the preparation and separation of para-xylene |
EP0031676A1 (en) * | 1979-12-19 | 1981-07-08 | Mobil Oil Corporation | Selective sorption by zeolites |
EP0531191A1 (en) * | 1991-09-05 | 1993-03-10 | Institut Français du Pétrole | Process and apparatus for the separation of paraxylene in aromatic hydrocarbures with adsorption in simulated moving bed and one crystallisation step |
FR2681066A1 (en) * | 1991-09-05 | 1993-03-12 | Inst Francais Du Petrole | Process and device for the separation of para-xylenes in a C8 aromatic hydrocarbon feedstock |
FR2693187A1 (en) * | 1992-07-06 | 1994-01-07 | Inst Francais Du Petrole | Sepn. and recovery of para-xylene |
FR2693186A1 (en) * | 1992-07-06 | 1994-01-07 | Inst Francais Du Petrole | Sepn. and recovery of para-xylene |
US6060634A (en) * | 1995-09-29 | 2000-05-09 | Institut Francais Du Petrole | Production of para-xylene from an effluent from paraselective toluene disproportionation using a crystallization process combined with simulated moving bed adsorption |
US6147272A (en) * | 1994-12-29 | 2000-11-14 | Institut Francais Du Petrole | Process for separating paraxylene comprising at least two crystallization stages at high temperature |
WO2002004391A1 (en) * | 2000-07-10 | 2002-01-17 | Bp Corporation North America Inc. | Pressure swing adsorption process for separating para-xylene and ethylbenzene from mixed c8 aromatics |
US6565653B2 (en) | 2001-05-08 | 2003-05-20 | Bp Corporation North America Inc. | Energy efficient process for producing high purity paraxylene |
US6573418B2 (en) | 2000-07-10 | 2003-06-03 | Bp Corporation North America Inc. | Process for production of para-xylene incorporating pressure swing adsorption and simulated moving bed adsorption |
WO2003059852A1 (en) * | 2002-01-09 | 2003-07-24 | Bp Corporation North America Inc. | Para-xylene and ethylbenzene separation from mixed c8 aromatics |
US6627783B2 (en) | 2000-07-10 | 2003-09-30 | Bp Corporation North America Inc. | Pressure swing adsorption process for separating para-xylene and ethylbenzene from mixed C8 aromatics |
US7122496B2 (en) | 2003-05-01 | 2006-10-17 | Bp Corporation North America Inc. | Para-xylene selective adsorbent compositions and methods |
US7271305B2 (en) | 2003-05-01 | 2007-09-18 | Bp Corporation North America Inc. | Method of obtaining para-xylene |
KR100799513B1 (en) | 2001-08-21 | 2008-01-31 | 더 스탠다드 오일 캄파니 | Improved operation of heads column in acrylonitrile production |
WO2011119808A1 (en) * | 2010-03-25 | 2011-09-29 | Exxonmobil Research And Engineering Company | Method of protecting a solid adsorbent and a protected solid adsorbent |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4899017A (en) * | 1987-07-27 | 1990-02-06 | Mobil Oil Corporation | Process for the selective separation of para-xylene from C8 aromatic mixtures |
-
1973
- 1973-11-06 CA CA185,091A patent/CA1059928A/en not_active Expired
- 1973-11-14 AU AU62466/73A patent/AU6246673A/en not_active Expired
- 1973-11-19 JP JP12930673A patent/JPS5046631A/ja active Pending
- 1973-11-19 GB GB5361273A patent/GB1420796A/en not_active Expired
- 1973-11-27 BE BE138237A patent/BE807878A/en unknown
- 1973-11-27 IT IT521673A patent/IT1001436B/en active
- 1973-11-28 DE DE19732359378 patent/DE2359378A1/en active Pending
- 1973-11-28 NL NL7316302A patent/NL7316302A/xx not_active Application Discontinuation
Cited By (27)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0003622A1 (en) * | 1978-02-07 | 1979-08-22 | Shell Internationale Researchmaatschappij B.V. | Process for the preparation and separation of para-xylene |
EP0031676A1 (en) * | 1979-12-19 | 1981-07-08 | Mobil Oil Corporation | Selective sorption by zeolites |
US5922924A (en) * | 1991-09-05 | 1999-07-13 | Institut Français Du Petrole | Process for the separation of p-xylene in C8 aromatic hydrocarbons with a simulated moving bed adsorption and a crystallization |
EP0531191A1 (en) * | 1991-09-05 | 1993-03-10 | Institut Français du Pétrole | Process and apparatus for the separation of paraxylene in aromatic hydrocarbures with adsorption in simulated moving bed and one crystallisation step |
FR2681066A1 (en) * | 1991-09-05 | 1993-03-12 | Inst Francais Du Petrole | Process and device for the separation of para-xylenes in a C8 aromatic hydrocarbon feedstock |
US5401476A (en) * | 1991-09-05 | 1995-03-28 | Institut Francais Du Petrole | Apparatus for the separation of p-xylene in C8 aromatic hydrocarbons with a simulated moving bed adsorption and a crystallization |
US5284992A (en) * | 1991-09-05 | 1994-02-08 | Institut Francais Du Petrole | Process and apparatus for the separation of p-xylene in C8 aromatic hydrocarbons with a simulated moving bed absorption and a crystallization |
FR2693186A1 (en) * | 1992-07-06 | 1994-01-07 | Inst Francais Du Petrole | Sepn. and recovery of para-xylene |
FR2693187A1 (en) * | 1992-07-06 | 1994-01-07 | Inst Francais Du Petrole | Sepn. and recovery of para-xylene |
US6147272A (en) * | 1994-12-29 | 2000-11-14 | Institut Francais Du Petrole | Process for separating paraxylene comprising at least two crystallization stages at high temperature |
US6060634A (en) * | 1995-09-29 | 2000-05-09 | Institut Francais Du Petrole | Production of para-xylene from an effluent from paraselective toluene disproportionation using a crystallization process combined with simulated moving bed adsorption |
US6689929B2 (en) | 2000-07-10 | 2004-02-10 | Bp Corporation North America Inc. | Process for the production of para-xylene using toluene feeds and pressure swing adsorption |
WO2002004391A1 (en) * | 2000-07-10 | 2002-01-17 | Bp Corporation North America Inc. | Pressure swing adsorption process for separating para-xylene and ethylbenzene from mixed c8 aromatics |
US6573418B2 (en) | 2000-07-10 | 2003-06-03 | Bp Corporation North America Inc. | Process for production of para-xylene incorporating pressure swing adsorption and simulated moving bed adsorption |
KR100881876B1 (en) | 2000-07-10 | 2009-02-06 | 비피 코포레이션 노쓰 아메리카 인코포레이티드 | Pressure swing adsorption process for separating para-xylene and ethylbenzene from mixed c8 aromatics |
US6600083B2 (en) | 2000-07-10 | 2003-07-29 | Bp Corporation North America Inc. | Para-xylene production process integrating pressure swing adsorption and crystallization |
US6627783B2 (en) | 2000-07-10 | 2003-09-30 | Bp Corporation North America Inc. | Pressure swing adsorption process for separating para-xylene and ethylbenzene from mixed C8 aromatics |
US6565653B2 (en) | 2001-05-08 | 2003-05-20 | Bp Corporation North America Inc. | Energy efficient process for producing high purity paraxylene |
KR100799513B1 (en) | 2001-08-21 | 2008-01-31 | 더 스탠다드 오일 캄파니 | Improved operation of heads column in acrylonitrile production |
WO2003059852A1 (en) * | 2002-01-09 | 2003-07-24 | Bp Corporation North America Inc. | Para-xylene and ethylbenzene separation from mixed c8 aromatics |
US7122496B2 (en) | 2003-05-01 | 2006-10-17 | Bp Corporation North America Inc. | Para-xylene selective adsorbent compositions and methods |
US7271305B2 (en) | 2003-05-01 | 2007-09-18 | Bp Corporation North America Inc. | Method of obtaining para-xylene |
WO2011119808A1 (en) * | 2010-03-25 | 2011-09-29 | Exxonmobil Research And Engineering Company | Method of protecting a solid adsorbent and a protected solid adsorbent |
CN102971071A (en) * | 2010-03-25 | 2013-03-13 | 埃克森美孚研究工程公司 | Method of protecting a solid adsorbent and a protected solid adsorbent |
US8500887B2 (en) | 2010-03-25 | 2013-08-06 | Exxonmobil Research And Engineering Company | Method of protecting a solid adsorbent and a protected solid adsorbent |
US8814986B2 (en) | 2010-03-25 | 2014-08-26 | ExxonMobil Research and Egineering Company | Method of protecting a solid adsorbent and a protected solid adsorbent |
CN102971071B (en) * | 2010-03-25 | 2015-09-02 | 埃克森美孚研究工程公司 | The method of protection solid absorbent and shielded solid absorbent |
Also Published As
Publication number | Publication date |
---|---|
BE807878A (en) | 1974-05-27 |
DE2359378A1 (en) | 1974-05-30 |
IT1001436B (en) | 1976-04-20 |
AU6246673A (en) | 1975-05-15 |
CA1059928A (en) | 1979-08-07 |
NL7316302A (en) | 1974-05-30 |
JPS5046631A (en) | 1975-04-25 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PCNP | Patent ceased through non-payment of renewal fee |