MX2015015930A - Proceso y aparato para enfriar coque. - Google Patents

Proceso y aparato para enfriar coque.

Info

Publication number
MX2015015930A
MX2015015930A MX2015015930A MX2015015930A MX2015015930A MX 2015015930 A MX2015015930 A MX 2015015930A MX 2015015930 A MX2015015930 A MX 2015015930A MX 2015015930 A MX2015015930 A MX 2015015930A MX 2015015930 A MX2015015930 A MX 2015015930A
Authority
MX
Mexico
Prior art keywords
coke
flow
water
equal
temperature
Prior art date
Application number
MX2015015930A
Other languages
English (en)
Other versions
MX363401B (es
Inventor
Giuseppina Cerea
Original Assignee
Ambiente E Nutrizione Srl
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 Ambiente E Nutrizione Srl filed Critical Ambiente E Nutrizione Srl
Publication of MX2015015930A publication Critical patent/MX2015015930A/es
Publication of MX363401B publication Critical patent/MX363401B/es

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B39/00—Cooling or quenching coke
    • C10B39/02—Dry cooling outside the oven
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B39/00—Cooling or quenching coke
    • C10B39/04—Wet quenching
    • C10B39/08—Coke-quenching towers
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B39/00—Cooling or quenching coke
    • C10B39/04—Wet quenching
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B39/00—Cooling or quenching coke
    • C10B39/10—Cooling or quenching coke combined with agitating means, e.g. rotating tables or drums
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B39/00—Cooling or quenching coke
    • C10B39/12—Cooling or quenching coke combined with conveying means
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L9/00—Treating solid fuels to improve their combustion
    • C10L9/08—Treating solid fuels to improve their combustion by heat treatments, e.g. calcining
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D15/00—Handling or treating discharged material; Supports or receiving chambers therefor
    • F27D15/02—Cooling
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D15/00—Handling or treating discharged material; Supports or receiving chambers therefor
    • F27D15/02—Cooling
    • F27D15/0286—Cooling in a vertical, e.g. annular, shaft
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28C—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
    • F28C3/00—Other direct-contact heat-exchange apparatus
    • F28C3/10—Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material
    • F28C3/12—Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material the heat-exchange medium being a particulate material and a gas, vapour, or liquid
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D21/0001—Recuperative heat exchangers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/0041—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for only one medium being tubes having parts touching each other or tubes assembled in panel form
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/10—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically
    • F28D7/106—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically consisting of two coaxial conduits or modules of two coaxial conduits
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/06—Heat exchange, direct or indirect
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0045—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for granular materials
    • 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
    • Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Thermal Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Combustion & Propulsion (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Coke Industry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)

Abstract

Se describe un método para enfriar coque procedente de la destilación de carbón y que tiene una temperatura mayor o igual a 900°C, que comprende las etapas de: a) disminuir la temperatura tal coque, a aproximadamente 700-300°C, mediante intercambio de calor con un fluido, a través de las paredes de un material térmicamente conductor, interpuesto entre el coque y el fluido, b) alimentar un flujo continuo de tal coque a aproximadamente 700-300°C a un turbo-enfriador (T), que comprende un cuerpo tubular cilíndrico (18), cerrado en extremos opuestos mediante respectivas placas del extremo (19,20), provisto con un encamisado de enfriamiento opcional (21) para la pared interna del mismo, por lo menos una abertura de entrada (9) para el coque, por lo menos una abertura de entrada (10, 15, 16 ) para agua, por lo menos una abertura de descarga (11, 12) y un rotor, soportado giratoriamente en el cuerpo tubular cilíndrico (5) y que comprende un árbol (13) provisto con elementos (14) que se proyectan radialmente desde tal árbol, aptos para la manipulación y el avance del coque; c) alimentar un flujo continuo de agua a una temperatura menor o igual a 100°C al turbo-enfriador (T), a través de tal por lo menos una abertura de entrada (10, 15, 16) y someter el flujo de coque y agua a la acción del rotor, que hace avanzar el coque hacia tal por lo menos una abertura de descarga (11); d) descargar continuamente de la por lo menos una abertura de descarga (11, 12) un flujo de coque a una temperatura menor o igual a 200°C y un flujo de vapor de agua.
MX2015015930A 2013-05-21 2014-05-21 Proceso y aparato para enfriar coque. MX363401B (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IT000826A ITMI20130826A1 (it) 2013-05-21 2013-05-21 Procedimento per lo spegnimento di coke
PCT/IB2014/061577 WO2014188346A1 (en) 2013-05-21 2014-05-21 A process and apparatus for quenching coke

Publications (2)

Publication Number Publication Date
MX2015015930A true MX2015015930A (es) 2016-06-28
MX363401B MX363401B (es) 2019-03-22

Family

ID=48670712

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2015015930A MX363401B (es) 2013-05-21 2014-05-21 Proceso y aparato para enfriar coque.

Country Status (11)

Country Link
US (1) US9567529B2 (es)
EP (1) EP2999768B1 (es)
JP (1) JP6377140B2 (es)
KR (1) KR102159297B1 (es)
CN (1) CN105264045B (es)
BR (1) BR112015029262A2 (es)
IT (1) ITMI20130826A1 (es)
MX (1) MX363401B (es)
RU (1) RU2669605C9 (es)
UA (1) UA116658C2 (es)
WO (1) WO2014188346A1 (es)

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3265740B1 (en) 2015-03-03 2018-12-05 Johnson Matthey Process Technologies, Inc. Heat exchanger
CN106010591A (zh) * 2016-06-30 2016-10-12 中国重型机械研究院股份公司 一种高温粉焦有机热载体余热回收系统
CN107779210A (zh) * 2016-08-31 2018-03-09 邢台旭阳科技有限公司 一种湿法熄焦系统及熄焦蒸汽回收的方法
CN108329950A (zh) * 2018-02-24 2018-07-27 余军 生物质活性炭的输送器
CN108998054A (zh) * 2018-08-01 2018-12-14 青岛京润石化设计研究院有限公司 一种流化床煤焦粉冷却方法
CN110835543B (zh) * 2018-08-16 2021-02-12 内蒙古万众炜业科技环保股份公司 兰炭余氨去除装置及其使用方法
CN109575959A (zh) * 2018-12-10 2019-04-05 五冶集团上海有限公司 炼焦工业中红焦炭的熄焦装置及其使用方法
CA3144601A1 (en) * 2019-06-24 2020-12-30 Kellogg Brown & Root Llc Integrated desolidification for solid-containing residues
CN110437850A (zh) * 2019-08-23 2019-11-12 西安华江环保科技股份有限公司 一种干法熄焦双超发电循环水冷却系统
CN110734778B (zh) * 2019-11-12 2021-01-22 佛山科学技术学院 一种有机质微波热解炭化装置
CN112179183B (zh) * 2020-08-24 2021-11-19 西安交通大学 一种用于电石余热回收的高效冷却装置
CN112127664A (zh) * 2020-09-22 2020-12-25 中国五冶集团有限公司 熄焦塔室复合墙结构及其施工方法
CN116925790B (zh) * 2023-09-18 2023-11-24 太原市凯特嘉机械有限公司 一种干熄焦装置、干熄焦系统和干熄焦工艺

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Also Published As

Publication number Publication date
RU2669605C9 (ru) 2019-01-17
ITMI20130826A1 (it) 2014-11-22
UA116658C2 (uk) 2018-04-25
RU2015149284A (ru) 2017-06-22
MX363401B (es) 2019-03-22
BR112015029262A2 (pt) 2017-07-25
US9567529B2 (en) 2017-02-14
CN105264045A (zh) 2016-01-20
EP2999768B1 (en) 2017-10-11
US20160145495A1 (en) 2016-05-26
CN105264045B (zh) 2017-10-10
JP6377140B2 (ja) 2018-08-22
WO2014188346A1 (en) 2014-11-27
JP2016522286A (ja) 2016-07-28
EP2999768A1 (en) 2016-03-30
KR102159297B1 (ko) 2020-09-24
KR20160012178A (ko) 2016-02-02
RU2669605C2 (ru) 2018-10-12

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