AR088302A1 - METHOD FOR DRY COCONUT TEMPERATURE BY MEANS OF VAPOR WITH FURTHER USE OF SYNTHESIS GAS PRODUCED - Google Patents

METHOD FOR DRY COCONUT TEMPERATURE BY MEANS OF VAPOR WITH FURTHER USE OF SYNTHESIS GAS PRODUCED

Info

Publication number
AR088302A1
AR088302A1 ARP120103789A ARP120103789A AR088302A1 AR 088302 A1 AR088302 A1 AR 088302A1 AR P120103789 A ARP120103789 A AR P120103789A AR P120103789 A ARP120103789 A AR P120103789A AR 088302 A1 AR088302 A1 AR 088302A1
Authority
AR
Argentina
Prior art keywords
synthesis gas
dry
coking
gas produced
coke
Prior art date
Application number
ARP120103789A
Other languages
Spanish (es)
Original Assignee
Thyssenkrupp Uhde Gmbh
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 Thyssenkrupp Uhde Gmbh filed Critical Thyssenkrupp Uhde Gmbh
Publication of AR088302A1 publication Critical patent/AR088302A1/en

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
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
    • C01B3/12—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/50—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/50—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
    • C01B3/56—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by contacting with solids; Regeneration of used solids
    • 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
    • C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
    • C10B49/02—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/58—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels combined with pre-distillation of the fuel
    • C10J3/60—Processes
    • C10J3/64—Processes with decomposition of the distillation products
    • C10J3/66—Processes with decomposition of the distillation products by introducing them into the gasification zone
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K3/00—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K3/00—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide
    • C10K3/001—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide by thermal treatment
    • C10K3/003—Reducing the tar content
    • C10K3/006—Reducing the tar content by steam reforming
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/0283—Processes for making hydrogen or synthesis gas containing a CO-shift step, i.e. a water gas shift step
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • C01B2203/042—Purification by adsorption on solids
    • C01B2203/043—Regenerative adsorption process in two or more beds, one for adsorption, the other for regeneration
    • 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

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Coke Industry (AREA)
  • Industrial Gases (AREA)

Abstract

La presente se refiere a un método para el templado en seco de coque por medio de vapor con posterior uso del gas de síntesis generado, dicho método incluye la coquización cíclica de carbón al coque enviando un dispositivo de templado después de descargarlo del horno de coque y el vapor se introduce en el dispositivo de templado para el templado en seco, creando así gas de síntesis compuesto de monóxido de carbono (CO) y hidrógeno (H₂) por medio de una reacción de agua-gas y el gas de síntesis producido se incorpora para una aplicación posterior. Este método permite usar el calor generado durante la coquización para la producción de gas de síntesis útil que, a su vez, se puede usar para un fin posterior o en el proceso de calentamiento, logrando así en total un equilibrio de calor extremadamente uniforme a lo largo de todo el proceso.This refers to a method for dry coking of coke by means of steam with subsequent use of the generated synthesis gas, said method includes cyclic coking of coal to coke by sending a tempering device after discharge from the coke oven and The steam is introduced into the tempering device for dry tempering, thus creating synthesis gas composed of carbon monoxide (CO) and hydrogen (H₂) by means of a water-gas reaction and the synthesis gas produced is incorporated for a later application. This method makes it possible to use the heat generated during coking for the production of useful synthesis gas which, in turn, can be used for a later purpose or in the heating process, thus achieving in total an extremely uniform heat balance at throughout the entire process

ARP120103789A 2011-10-12 2012-10-11 METHOD FOR DRY COCONUT TEMPERATURE BY MEANS OF VAPOR WITH FURTHER USE OF SYNTHESIS GAS PRODUCED AR088302A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE102011115698A DE102011115698A1 (en) 2011-10-12 2011-10-12 Process for the dry cooling of coke with steam with subsequent use of the synthesis gas produced

Publications (1)

Publication Number Publication Date
AR088302A1 true AR088302A1 (en) 2014-05-21

Family

ID=47022619

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP120103789A AR088302A1 (en) 2011-10-12 2012-10-11 METHOD FOR DRY COCONUT TEMPERATURE BY MEANS OF VAPOR WITH FURTHER USE OF SYNTHESIS GAS PRODUCED

Country Status (7)

Country Link
US (1) US20140352207A1 (en)
EP (1) EP2766453A1 (en)
AR (1) AR088302A1 (en)
DE (1) DE102011115698A1 (en)
RU (1) RU2605125C2 (en)
TW (1) TW201335353A (en)
WO (1) WO2013053427A1 (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102011115699A1 (en) * 2011-10-12 2013-04-18 Thyssenkrupp Uhde Gmbh Process for the dry cooling of coke with carbon dioxide with subsequent use of the carbon monoxide produced
CN103881735B (en) * 2014-01-03 2016-03-30 科利特环能科技（大连）有限公司 Prevent red incipient scorch from undermining the extinguishing technique reclaiming coke heat energy
CN104673333B (en) * 2015-02-03 2017-10-10 天津大学 Quenching and the method and apparatus recovered energy
CN105754618B (en) * 2016-03-30 2018-09-28 沈阳环境科学研究院 A kind of gas-phase chemical reduction method extinguishing technique method
CN106479542B (en) * 2016-10-27 2019-08-20 武汉钢铁有限公司 The water-gas preparation process to be dehumidified based on Dry Quenching and coking coal
CN111019680A (en) * 2019-12-10 2020-04-17 上海交通大学 Method for promoting coal coking and improving gas yield and quality

Family Cites Families (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE375785C (en) * 1921-01-03 1923-05-18 Sulzer Akt Ges Geb Process for cooling glowing coke
DE510328C (en) * 1929-02-15 1930-10-18 Otto & Co Gmbh Dr C Device for generating water gas from glowing coke
GB347601A (en) 1930-01-28 1931-04-28 Daniel Tyrer Improvements in and relating to the cooling of coke and obtaining a nitrogen hydrogen mixture
DE2435500A1 (en) 1974-07-24 1976-02-12 Hugo Dr Ing Schaefer Coking coal preheating system - using waste heat from dry coke quenching antechamber and chamber with steam jackets
US3959084A (en) * 1974-09-25 1976-05-25 Dravo Corporation Process for cooling of coke
AT361892B (en) * 1975-06-13 1981-04-10 Waagner Biro Ag METHOD AND DEVICE FOR COOLING HOT SHEET GOODS, ESPECIALLY FOR DRYING AND DELETING HOT COOK
SU802354A1 (en) * 1977-03-01 1981-02-07 Украинский Научно-Исследовательскийуглехимический Институт Method and device for dry coke quenching and producing hydrogen- and carbonmonoxide-containing gases
DE3030969A1 (en) 1980-08-16 1982-04-01 Dr. C. Otto & Comp. Gmbh, 4630 Bochum Dry coke quenching system - preceded by screening in two or three size ranges for separate bolting chambers
DE3032212C2 (en) * 1980-08-27 1986-09-18 Carl Still Gmbh & Co Kg, 4350 Recklinghausen Process for the production of H 2 and CO-containing gases by gasification of coke
JPS5770186A (en) * 1980-10-21 1982-04-30 Kawasaki Steel Corp Preparation of coke gas utilizing quenching equipment of coke oven
DE3112256C2 (en) * 1981-03-27 1987-02-12 Hartung, Kuhn & Co Maschinenfabrik GmbH, 4000 Düsseldorf Process for utilizing waste heat and for obtaining water gas from the cooling of glowing coke ejected from a chamber furnace
US4627174A (en) * 1982-02-04 1986-12-09 Bergwerksverband Gmbh Process and system for the dry quenching of coke
DE3217146A1 (en) 1982-05-07 1983-11-10 Krupp-Koppers Gmbh, 4300 Essen Device for dedusting circulating gas of a dry coke-cooling installation
DE3235261C2 (en) * 1982-09-23 1984-08-02 Hartung, Kuhn & Co Maschinenfabrik GmbH, 4000 Düsseldorf Process and device for using waste heat and for obtaining water gas when cooling coke
JPS60110784A (en) * 1983-11-22 1985-06-17 Sumitomo Metal Ind Ltd Method for treating exhaust gas form dry quenching furnace for coke
DE3441322C1 (en) 1984-11-12 1986-05-28 Bergwerksverband Gmbh, 4300 Essen Process and device for dry coke cooling
DE3739789A1 (en) 1987-11-24 1989-06-08 Ruhrkohle Ag COCK DRY COOLING
DE3941453C1 (en) 1989-12-15 1991-06-20 Didier Ofu Engineering Gmbh
DE19614482C1 (en) 1996-04-12 1997-06-26 Krupp Koppers Gmbh Coke quenching plant with simplified water delivery systems
DE102004062687A1 (en) 2004-12-21 2006-06-29 Uhde Gmbh Process for generating hydrogen and energy from synthesis gas
DE102009022509B4 (en) * 2009-05-25 2015-03-12 Thyssenkrupp Industrial Solutions Ag Process for the production of synthesis gas
CN101845307A (en) * 2010-06-02 2010-09-29 北京硕人海泰能源环境技术研究院 Energy-saving and emission-reducing device for coke dry quenching and energy-saving and emission-reducing coking process using same

Also Published As

Publication number Publication date
US20140352207A1 (en) 2014-12-04
RU2014118737A (en) 2015-11-20
DE102011115698A1 (en) 2013-04-18
TW201335353A (en) 2013-09-01
EP2766453A1 (en) 2014-08-20
WO2013053427A1 (en) 2013-04-18
RU2605125C2 (en) 2016-12-20

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