ES2065397T3 - Procedimiento de integracion de calor. - Google Patents

Procedimiento de integracion de calor.

Info

Publication number
ES2065397T3
ES2065397T3 ES89311151T ES89311151T ES2065397T3 ES 2065397 T3 ES2065397 T3 ES 2065397T3 ES 89311151 T ES89311151 T ES 89311151T ES 89311151 T ES89311151 T ES 89311151T ES 2065397 T3 ES2065397 T3 ES 2065397T3
Authority
ES
Spain
Prior art keywords
methanol
refined
water
mtbe
overheated
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 - Lifetime
Application number
ES89311151T
Other languages
English (en)
Inventor
Lawrence A Smith Jr
Edward M Jones Jr
Dennis Hearn
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chemical Research and Licensing Co
Original Assignee
Chemical Research and Licensing Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Chemical Research and Licensing Co filed Critical Chemical Research and Licensing Co
Application granted granted Critical
Publication of ES2065397T3 publication Critical patent/ES2065397T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C43/00Ethers; Compounds having groups, groups or groups
    • C07C43/02Ethers
    • C07C43/03Ethers having all ether-oxygen atoms bound to acyclic carbon atoms
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C41/00Preparation of ethers; Preparation of compounds having groups, groups or groups
    • C07C41/01Preparation of ethers
    • C07C41/34Separation; Purification; Stabilisation; Use of additives
    • C07C41/40Separation; Purification; Stabilisation; Use of additives by change of physical state, e.g. by crystallisation
    • C07C41/42Separation; Purification; Stabilisation; Use of additives by change of physical state, e.g. by crystallisation by distillation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C41/00Preparation of ethers; Preparation of compounds having groups, groups or groups
    • C07C41/01Preparation of ethers
    • C07C41/05Preparation of ethers by addition of compounds to unsaturated compounds
    • C07C41/06Preparation of ethers by addition of compounds to unsaturated compounds by addition of organic compounds only
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency

Abstract

UNA PARTE DEL CALOR DE VAPORIZACION, REQUERIDO PARA SEPARAR Y RECUPERAR METANOL DE AGUA DE LAVAR USADA PARA QUITAR METANOL DE UN C4 REFINADO RESULTANTE DE LA REACCION DE ISOBUTENO QUE CONTIENE HIDROCARBONOS C4 Y METANOL PARA PRODUCIR MTBE ES RECUPERADO POR CONDUCIR LA DESTILACION DE LA MEZCLA DE METANOL/AGUA A UNA PRESION DE 40 A 60 PSIG, POR LO CUAL INCREMENTAR LA TEMPERATURA DEL METANOL POR ENCIMA DE 104 A 114 C Y USAR LA REACCION EFLUYENTE DEL REACTOR MTBE PARA ENFRIAR Y CONDENSAR EL METANOL SOBRECALENTADO, DICHO REACTOR EFLUYENTE ES CORRESPONDIENTEMENTE CALENTADO ANTES DE ENTRAR DENTRO DE UNA TORRE DEBUTANIZADORA DONDE EL C4 NO REACCIONADO Y EL METANOL SON QUITADOS COMO UN PRODUCTO MTBE Y REFINADO RECUPERADO. ES ESTE REFINADO EL QUE ES LAVADO CON AGUA PARA RECUPERAR EL METANOL NO REACCIONADO, CON LA MEZCLA METANOL/AGUA SIENDO DESTILADA COMO SE HA PUESTO SUCESIVAMENTE ANTES. EN OTRO CASO UNA CORRIENTE QUE TIENE UNA TEMPERATURA MAS BAJA QUE EL METANOL SOBRECALENTADO ES EXTRAIDO DEL DEBUTANIZADOR Y USADO PARA ENFRIAR EL METANOL SOBRECALENTADO, ENTONCES LA CORRIENTE CALENTADA CORRESPONDIENTEMENTE VUELVE AL DEBUTANIZADOR.
ES89311151T 1988-10-28 1989-10-27 Procedimiento de integracion de calor. Expired - Lifetime ES2065397T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US07/263,812 US4918243A (en) 1988-10-28 1988-10-28 Heat integration process

Publications (1)

Publication Number Publication Date
ES2065397T3 true ES2065397T3 (es) 1995-02-16

Family

ID=23003325

Family Applications (1)

Application Number Title Priority Date Filing Date
ES89311151T Expired - Lifetime ES2065397T3 (es) 1988-10-28 1989-10-27 Procedimiento de integracion de calor.

Country Status (8)

Country Link
US (1) US4918243A (es)
EP (1) EP0366501B1 (es)
JP (1) JPH02243642A (es)
KR (1) KR900006270A (es)
CA (1) CA2001755A1 (es)
DE (1) DE68919805T2 (es)
ES (1) ES2065397T3 (es)
MY (1) MY105606A (es)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5144085A (en) * 1990-03-28 1992-09-01 Mobil Oil Corporation Feedstock dewatering and etherification of crude ethanol
US5149892A (en) * 1991-10-22 1992-09-22 Ppg Industries, Inc. Chlorinated benzenes
AU654757B2 (en) 1992-02-10 1994-11-17 Chemical Research & Licensing Company Selective hydrogenation of C5 streams
CA2111018A1 (en) * 1993-01-06 1994-07-07 Jacob N. Rubin Integrated mtbe process
US5336841A (en) * 1993-04-05 1994-08-09 Chemical Research & Licensing Company Oxygenate removal in MTBE process
US5430197A (en) * 1994-02-22 1995-07-04 Chemica Research & Licensing Company Recovery of alcohol from hydrocarbon streams
US5600024A (en) * 1995-07-26 1997-02-04 Phillips Petroleum Company Enhanced recovery of alcohol from an ether containing stream
CN101367696B (zh) * 2008-08-02 2013-04-24 中国石油兰州石油化工公司 一种甲基叔丁基醚尾气回收甲醇的方法
RS63920B1 (sr) 2018-04-11 2023-02-28 Lummus Technology Inc Strukturirano pakovanje za katalitičku destilaciju
US20230271907A1 (en) * 2020-07-21 2023-08-31 Sabic Global Technologies B.V. System and method for production of mtbe

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4198530A (en) * 1978-06-29 1980-04-15 Atlantic Richfield Company Production of tertiary butyl methyl ether
FR2455019A1 (fr) * 1979-04-24 1980-11-21 Inst Francais Du Petrole Procede de production de methyltertiobutyl ether a partir de methanol et d'isobutene
US4336407A (en) * 1980-02-25 1982-06-22 Chemical Research & Licensing Company Catalytic distillation process

Also Published As

Publication number Publication date
JPH02243642A (ja) 1990-09-27
EP0366501B1 (en) 1994-12-07
DE68919805T2 (de) 1995-05-04
MY105606A (en) 1994-11-30
EP0366501A3 (en) 1991-05-22
US4918243A (en) 1990-04-17
EP0366501A2 (en) 1990-05-02
DE68919805D1 (de) 1995-01-19
CA2001755A1 (en) 1990-04-28
KR900006270A (ko) 1990-05-07

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