EA201690088A1 - Способ получения метанола в параллельных реакторах - Google Patents

Способ получения метанола в параллельных реакторах

Info

Publication number
EA201690088A1
EA201690088A1 EA201690088A EA201690088A EA201690088A1 EA 201690088 A1 EA201690088 A1 EA 201690088A1 EA 201690088 A EA201690088 A EA 201690088A EA 201690088 A EA201690088 A EA 201690088A EA 201690088 A1 EA201690088 A1 EA 201690088A1
Authority
EA
Eurasian Patent Office
Prior art keywords
methanol
methanol synthesis
effluent
synthesis reactor
reactor
Prior art date
Application number
EA201690088A
Other languages
English (en)
Other versions
EA031957B1 (ru
Inventor
Хассан Модарреси
Кристиан Викс
Original Assignee
Хальдор Топсёэ А/С
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 Хальдор Топсёэ А/С filed Critical Хальдор Топсёэ А/С
Publication of EA201690088A1 publication Critical patent/EA201690088A1/ru
Publication of EA031957B1 publication Critical patent/EA031957B1/ru

Links

Classifications

    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18—Stationary reactors having moving elements inside
    • B01J19/1856—Stationary reactors having moving elements inside placed in parallel
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/0292—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds with stationary packing material in the bed, e.g. bricks, wire rings, baffles
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0446—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
    • B01J8/0449—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds
    • B01J8/0453—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds the beds being superimposed one above the other
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/15—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
    • C07C29/151—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
    • C07C29/152—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases characterised by the reactor used
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
    • B01J2208/00274—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant vapours
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/02—Processes carried out in the presence of solid particles; Reactors therefor with stationary particles
    • B01J2208/023—Details
    • B01J2208/027—Beds
    • 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
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

Способ получения метанола в параллельных реакторах, включающий следующие этапы: (а) реакцию оксидов углерода и водорода в присутствии катализатора синтеза метанола в первом реакторе синтеза метанола с получением первого метанолсодержащего выходящего потока; (b) подачу и реакцию непрореагировавшего синтез-газа во втором реакторе синтеза метанола в присутствии катализатора синтеза метанола с получением второго метанолсодержащего выходящего потока, при этом первый реактор синтеза метанола и второй реактор синтеза метанола соединены параллельно; (с) объединение первого и второго выходящих потоков, и (d) охлаждение и сепарацию объединенного и охлажденного выходящего потока на метанолсодержащую жидкую фазу и непрореагировавший синтез-газ, при этом осуществляют непрямое охлаждение катализатора синтеза метанола в первом реакторе синтеза метанола с помощью кипящей воды и осуществляют прямое или непрямое охлаждение катализатора синтеза метанола во втором реакторе синтеза метанола с помощью непрореагировавшего синтез-газа перед конверсией во второй выходящий поток.
EA201690088A 2013-06-27 2014-05-15 Способ получения метанола в параллельных реакторах EA031957B1 (ru)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP13174010.2A EP2818458B1 (en) 2013-06-27 2013-06-27 Process for the preparation of methanol in parallel reactors
PCT/EP2014/059962 WO2014206635A1 (en) 2013-06-27 2014-05-15 Process for the preparation of methanol in parallel reactors

Publications (2)

Publication Number Publication Date
EA201690088A1 true EA201690088A1 (ru) 2016-07-29
EA031957B1 EA031957B1 (ru) 2019-03-29

Family

ID=48699611

Family Applications (1)

Application Number Title Priority Date Filing Date
EA201690088A EA031957B1 (ru) 2013-06-27 2014-05-15 Способ получения метанола в параллельных реакторах

Country Status (7)

Country Link
US (1) US9464014B2 (ru)
EP (1) EP2818458B1 (ru)
CN (2) CN111574324A (ru)
CA (1) CA2911306C (ru)
EA (1) EA031957B1 (ru)
PL (1) PL2818458T3 (ru)
WO (1) WO2014206635A1 (ru)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB201600794D0 (en) 2016-01-15 2016-03-02 Johnson Matthey Davy Technologies Ltd Methanol process
GB201600793D0 (en) * 2016-01-15 2016-03-02 Johnson Matthey Davy Technologies Ltd Methanol process
WO2018166872A1 (en) * 2017-03-12 2018-09-20 Haldor Topsøe A/S Co-production of methanol and ammonia
EP3596044B1 (en) * 2017-03-12 2023-07-19 Topsoe A/S Co-production of methanol, ammonia and urea
WO2021137172A1 (en) * 2020-01-02 2021-07-08 Sabic Global Technologies B.V. Process for methanol production from inert-rich synthesis gas
US20230391698A1 (en) 2020-11-17 2023-12-07 Total Energies Onetech Process for methanol synthesis from co2-rich syngas
WO2023154854A1 (en) * 2022-02-14 2023-08-17 Cribl, Inc. Edge-based data collection system for an observability pipeline system

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51131813A (en) 1975-05-07 1976-11-16 Mitsubishi Gas Chem Co Inc Process for methanol production
US4766154A (en) * 1987-02-06 1988-08-23 Air Products And Chemicals, Inc. Liquid phase methanol reactor staging process for the production of methanol
DE4004862A1 (de) 1990-02-16 1991-08-22 Uhde Gmbh Methanolsynthese mit frischgaszufuhr
DE4416425A1 (de) * 1994-05-10 1995-11-16 Metallgesellschaft Ag Verfahren zur Erzeugung von Methanol
DE19605572A1 (de) 1996-02-15 1997-08-21 Metallgesellschaft Ag Verfahren zum Erzeugen von Methanol
GB0418654D0 (en) * 2004-08-20 2004-09-22 Davy Process Techn Ltd Process
DE102007040707B4 (de) 2007-08-29 2012-05-16 Lurgi Gmbh Verfahren und Anlage zur Herstellung von Methanol
DE102008049621B4 (de) 2008-09-30 2011-12-22 Lurgi Gmbh Verfahren und Anlage zur Herstellung von Methanol
DE102010008857A1 (de) 2010-02-22 2011-08-25 Lurgi GmbH, 60439 Verfahren zur Herstellung von Methanol

Also Published As

Publication number Publication date
EP2818458B1 (en) 2016-10-19
CN105392762A (zh) 2016-03-09
CA2911306C (en) 2021-06-15
US9464014B2 (en) 2016-10-11
CA2911306A1 (en) 2014-12-31
EA031957B1 (ru) 2019-03-29
EP2818458A1 (en) 2014-12-31
PL2818458T3 (pl) 2017-07-31
US20160107961A1 (en) 2016-04-21
CN111574324A (zh) 2020-08-25
WO2014206635A1 (en) 2014-12-31

Similar Documents

Publication Publication Date Title
EA201690088A1 (ru) Способ получения метанола в параллельных реакторах
EA201590793A1 (ru) Способ получения углеводородов
RU2014135473A (ru) Прямой синтез дмэ в условиях равновесия
GB2511266A (en) Conversion of carbon dioxide to hydrocarbons via hydrogenation
EA201390065A1 (ru) Способ получения этанола и высших спиртов
EA201691256A1 (ru) Способ производства этанола совместно с метанолом
EA201891603A1 (ru) Способ получения метанола
EA201391404A1 (ru) Способ производства олефинов
EA201600532A1 (ru) Способ получения ароматических углеводородов из природного газа и установка для его осуществления
AR083197A1 (es) Produccion de acido acetico con alta tasa de conversion
TR201911205T4 (tr) H2 ve C02'nin biyometanlaştırılması için yöntem.
MY195834A (en) Process For Producing Dimethyl Carbonate
EA201301250A1 (ru) Способ обработки синтез-газа и система, использующая медный катализатор в двухступенчатых реакциях при 475-525°c и 250-290°c
JP2018165388A (ja) 水の利用方法及び水電解システム
WO2013041516A3 (en) Cooled reactor for the production of dimethyl ether from methanol
EA201691757A1 (ru) Способ получения синтез-газа
EA201390650A1 (ru) Способ селективного получения 1-пропанола, изобутанола и других с+ спиртов из синтез-газа и метанола
MY188858A (en) Process for producing ammonia synthesis gas
MY158397A (en) Process and apparatus for producing dimethyl ether from methanol
CL2011002471A1 (es) Procedimiento industrial para la obtencion de alcoholes inferiores a partir de energia solar.
MX2012008965A (es) Proceso para la preparacion de eter dimetilico.
GB2489362A (en) Two stage process for the conversion of synthesis gas using a cobalt catalyst the first stage and a supported ruthenium in the second stage
EA201290314A1 (ru) Сегментные реакторы для изменений производительности и обогащения при превращении гексафторида урана в диоксид урана
EA201590472A1 (ru) Способ получения диметилового эфира
MX2015008962A (es) Proceso continuo para la conversion de lignina a compuestos utiles.

Legal Events

Date Code Title Description
MM4A Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s)

Designated state(s): AM AZ KZ KG TJ