EA201270090A1 - Способ получения пара с использованием тепла, извлеченного из реакции полимеризации - Google Patents

Способ получения пара с использованием тепла, извлеченного из реакции полимеризации

Info

Publication number
EA201270090A1
EA201270090A1 EA201270090A EA201270090A EA201270090A1 EA 201270090 A1 EA201270090 A1 EA 201270090A1 EA 201270090 A EA201270090 A EA 201270090A EA 201270090 A EA201270090 A EA 201270090A EA 201270090 A1 EA201270090 A1 EA 201270090A1
Authority
EA
Eurasian Patent Office
Prior art keywords
polymerization reaction
cooling fluid
relates
absorption cycle
vapor
Prior art date
Application number
EA201270090A
Other languages
English (en)
Other versions
EA020963B1 (ru
Inventor
Пьерр Ван Грамбезен
Мурад Абуахи
Original Assignee
Тотал Петрокемикалз Ресерч Фелюи
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 Тотал Петрокемикалз Ресерч Фелюи filed Critical Тотал Петрокемикалз Ресерч Фелюи
Publication of EA201270090A1 publication Critical patent/EA201270090A1/ru
Publication of EA020963B1 publication Critical patent/EA020963B1/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
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/2455—Stationary reactors without moving elements inside provoking a loop type movement of the reactants
    • B01J19/246—Stationary reactors without moving elements inside provoking a loop type movement of the reactants internally, i.e. the mixture circulating inside the vessel such that the upward stream is separated physically from the downward stream(s)
    • 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
    • B01J19/1812—Tubular reactors
    • B01J19/1837—Loop-type reactors
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B1/00—Methods of steam generation characterised by form of heating method
    • F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
    • F22B1/16—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being hot liquid or hot vapour, e.g. waste liquid, waste vapour
    • 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
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B1/00—Methods of steam generation characterised by form of heating method
    • F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
    • F22B1/18—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
    • B01J2219/00094—Jackets
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F110/02—Ethene
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F210/00—Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F210/16—Copolymers of ethene with alpha-alkenes, e.g. EP rubbers
    • 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)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Energy (AREA)
  • Sustainable Development (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Combustion & Propulsion (AREA)
  • Polymerisation Methods In General (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

Настоящее изобретение относится к способу получения пара при помощи тепла, извлеченного из реакции полимеризации. В частности, настоящее изобретение относится к способу получения пара при помощи тепла, извлеченного из реакции полимеризации для получения полиолефинов, включающего этапы термического контактирования указанной реакции полимеризации с охлаждающей текучей средой таким образом, чтобы охлаждающая текучая среда удаляла тепло из указанной реакции; термического контактирования по меньшей мере части указанной охлаждающей текучей среды по меньшей мере с одним абсорбционным циклом, при этом передается тепло из охлаждающей текучей среды к указанному абсорбционному циклу, используя указанный абсорбционный цикл для получения пара из конденсата, причем охлаждающая текучая среда используется в качестве источника нагревания для нагрева по меньшей мере одного испарителя и по меньшей мере одного генератора, которые заключены по меньшей мере в одном абсорбционном цикле. Настоящее изобретение также относится к способу охлаждения реакции полимеризации при помощи раскрытого в данном документе способа. Указанное изобретение также относится к установке для получения полиолефинов.
EA201270090A 2009-07-01 2010-07-01 Способ получения пара с использованием тепла, извлеченного из реакции полимеризации EA020963B1 (ru)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP09164262A EP2281627A1 (en) 2009-07-01 2009-07-01 Process for producing steam using heat recovered from a polymerization reaction
PCT/EP2010/059393 WO2011000925A1 (en) 2009-07-01 2010-07-01 Process for producing steam using heat recovered from a polymerization reaction

Publications (2)

Publication Number Publication Date
EA201270090A1 true EA201270090A1 (ru) 2012-05-30
EA020963B1 EA020963B1 (ru) 2015-03-31

Family

ID=40996561

Family Applications (1)

Application Number Title Priority Date Filing Date
EA201270090A EA020963B1 (ru) 2009-07-01 2010-07-01 Способ получения пара с использованием тепла, извлеченного из реакции полимеризации

Country Status (13)

Country Link
US (2) US8436109B2 (ru)
EP (2) EP2281627A1 (ru)
KR (1) KR101344545B1 (ru)
CN (1) CN102548653B (ru)
BR (1) BRPI1011797B1 (ru)
EA (1) EA020963B1 (ru)
ES (1) ES2661239T3 (ru)
HU (1) HUE036689T2 (ru)
MX (1) MX2011013934A (ru)
PL (1) PL2448664T3 (ru)
PT (1) PT2448664T (ru)
TR (1) TR201802736T4 (ru)
WO (1) WO2011000925A1 (ru)

Families Citing this family (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2065641A3 (de) * 2007-11-28 2010-06-09 Siemens Aktiengesellschaft Verfahren zum Betrieben eines Durchlaufdampferzeugers sowie Zwangdurchlaufdampferzeuger
MX2012008436A (es) * 2010-02-05 2012-12-10 Total Petrochemicals Res Feluy Proceso para preparar poliolefina.
US9193105B1 (en) * 2011-08-31 2015-11-24 Consolidated Nuclear Security, LLC Casting fine grained, fully dense, strong inorganic materials
EP2615119B1 (en) * 2012-01-12 2016-10-26 Evonik Degussa GmbH Cooling neutralized acrylic acid by means of an absorption chiller
US9328963B2 (en) 2013-07-10 2016-05-03 Renmatix, Inc. Energy recovery when processing materials with reactive fluids
WO2015005918A1 (en) * 2013-07-10 2015-01-15 Renmatix, Inc. Energy recovery when processing materials with reactive fluids
EP3098549B1 (en) * 2015-05-26 2018-07-11 General Electric Technology GmbH Lignite drying with a heat recovery circuit
US9920658B2 (en) 2015-12-08 2018-03-20 Applied Research Associates, Inc. Dry cooling system using thermally induced vapor polymerization
US10752821B2 (en) 2015-12-08 2020-08-25 Applied Research Associates, Inc. Dry cooling systems using thermally induced polymerization
US10066142B2 (en) 2015-12-08 2018-09-04 Applied Research Associates, Inc. Dry cooling system using thermally induced vapor polymerization
US9702596B2 (en) * 2015-12-08 2017-07-11 Applied Research Associates, Inc. Dry cooling system using thermally induced vapor polymerization
US10487694B2 (en) 2015-12-08 2019-11-26 Applied Research Associates, Inc. Dry cooling system using thermally induced vapor polymerization
US10258953B2 (en) * 2016-08-05 2019-04-16 Covestro Llc Systems and processes for producing polyether polyols
JP6895024B2 (ja) 2018-03-29 2021-06-30 エックスワイゼット エナジー グループ、エルエルシー １次熱伝達ループ、発電サイクル・ループ、及び中間熱伝達ループを備える多重閉ループを使用して熱及び電力を生成するためのシステム及び方法
US11180587B2 (en) * 2019-12-13 2021-11-23 Chevron Phillips Chemical Company Lp Polymerization of propylene
WO2022125454A1 (en) 2020-12-07 2022-06-16 XYZ Energy Group, LLC Multiple loop power generation using super critical cycle fluid with split recuperator
CN113893794B (zh) * 2021-10-08 2022-06-28 江苏科利新材料有限公司 氯化聚乙烯的节能型生产系统
CN114225856A (zh) * 2021-12-01 2022-03-25 浙江智英石化技术有限公司 一种乙烯选择性齐聚生产1-己烯的装置及工艺
EP4269757A1 (en) 2022-04-28 2023-11-01 Borealis AG Method for recovering energy
EP4269758A1 (en) 2022-04-28 2023-11-01 Borealis AG Method for recovering energy

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT366069B (de) * 1978-04-18 1982-03-10 Union Carbide Corp Kontinuierliches niederdruck-gasphasenverfahren zur herstellung von festen teilchenfoermigen olefin-polymeren und fliessbettreaktor zur durchfuehrung des verfahrens
US5584193A (en) * 1994-04-26 1996-12-17 York International Corporation Absorption-type refrigeration systems and methods
ES2416314T3 (es) 2004-08-27 2013-07-31 Chevron Phillips Chemical Company Lp Procesos de producción de poliolefinas
CN101004303B (zh) * 2007-01-08 2010-05-19 李华玉 三级第一类吸收式热泵
EP2017291A1 (en) 2007-07-16 2009-01-21 Total Petrochemicals Research Feluy Method for optimizing energy efficiency in a polymerization process.
CN101261054A (zh) * 2007-12-29 2008-09-10 清华大学 一种大温升吸收式热泵机组

Also Published As

Publication number Publication date
EP2448664B1 (en) 2017-11-29
PT2448664T (pt) 2018-03-07
BRPI1011797B1 (pt) 2018-02-06
US20120088892A1 (en) 2012-04-12
CN102548653A (zh) 2012-07-04
KR20120028351A (ko) 2012-03-22
CN102548653B (zh) 2015-04-29
TR201802736T4 (tr) 2018-03-21
KR101344545B1 (ko) 2013-12-26
EP2281627A1 (en) 2011-02-09
WO2011000925A1 (en) 2011-01-06
US8436109B2 (en) 2013-05-07
ES2661239T3 (es) 2018-03-28
HUE036689T2 (hu) 2018-07-30
BRPI1011797A2 (pt) 2016-03-22
PL2448664T3 (pl) 2018-05-30
MX2011013934A (es) 2012-04-30
US8697819B2 (en) 2014-04-15
EP2448664A1 (en) 2012-05-09
US20130224078A1 (en) 2013-08-29
EA020963B1 (ru) 2015-03-31

Similar Documents

Publication Publication Date Title
EA201270090A1 (ru) Способ получения пара с использованием тепла, извлеченного из реакции полимеризации
WO2010143046A3 (en) Multi-level organic rankine cycle power system
WO2012138766A3 (en) System for generating power from a syngas fermentation process
WO2012048135A3 (en) Utilization of process heat by-product
WO2012050788A3 (en) Apparatus and process for producing superheated steam from a concentrating solar power plant
MX351110B (es) Aparatos y el procedimiento para la generación de energía mediante el ciclo orgánico de rankine.
EA201390286A1 (ru) Способ и устройство для генерации технологического пара и водяного пара питания котла в нагреваемом преобразующем реакторе для производства синтетического газа
WO2012048127A3 (en) Improving capacity and performance of process columns by overhead heat recovery into an organic rankine cycle for power generation
EA201491234A1 (ru) Способ и агрегат для получения азотной кислоты
EA201391352A1 (ru) Способ и система для регенерации тепловой энергии из пароосушителя
MY187861A (en) Method and system for drying biomass
MX2014009894A (es) Planta y metodo para aumentar la eficiencia de produccion de energia electrica.
WO2012066579A3 (en) Process for utilization of low pressure, low temperature steam from steam turbine for desalination of sea water
EA201591007A1 (ru) Рекуперация энергии и воды из полученного в процессе окисления под давлением пара из расширителя
BR112017024240A2 (pt) método para tratar gás de síntese, sistema de resfriamento para resfriar gás de síntese, e sistema de gaseificação para produção de gás de síntese
PE20180157A1 (es) Proceso para preparar un gas de sintesis y un dispositivo de enfriamiento de gas de sintesis
IN2012DN02614A (ru)
WO2012171877A3 (de) Solarthermische anlage mit wärmerohren
UA106328C2 (ru) Способ изводства механической и электрической энергии и система для его осуществления
TH130178B (th) การใช้ความร้อนในกระบวนการที่เป็นผลิตผลพลอยได้
RU2010124059A (ru) Способ работы тепловой электрической станции
TH149181B (th) วิธีการและอุปกรณ์สำหรับการผลิตสารละลายแอคเควียสของไซยาโนโพริดีน
RU2010124061A (ru) Способ работы тепловой электрической станции
RU2015109409A (ru) Способ работы котельной установки
GR20130100551A (el) Μια ενσωματωμενη διεργασια για την παραγωγη ηλεκτρικης ισχυος και σχετικη συσκευη

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 BY KZ KG MD TJ TM