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CL2008000120A1 - Reactor; y proceso para la preparacion continua de h2s por conversion de una mezcla reactante que contiene azufre gaseoso e hidrogeno sobre un catalizador y azufre fundido en la parte inferior del reactor que comprende que dicho catalizador esta disp - Google Patents

Reactor; y proceso para la preparacion continua de h2s por conversion de una mezcla reactante que contiene azufre gaseoso e hidrogeno sobre un catalizador y azufre fundido en la parte inferior del reactor que comprende que dicho catalizador esta disp

Info

Publication number
CL2008000120A1
CL2008000120A1 CL200800120A CL2008000120A CL2008000120A1 CL 2008000120 A1 CL2008000120 A1 CL 2008000120A1 CL 200800120 A CL200800120 A CL 200800120A CL 2008000120 A CL2008000120 A CL 2008000120A CL 2008000120 A1 CL2008000120 A1 CL 2008000120A1
Authority
CL
Chile
Prior art keywords
reactor
catalyst
hydrogen
sulfured
disp
Prior art date
Application number
CL200800120A
Other languages
English (en)
Inventor
Andreas Wolfert
Harald Jachow
Heinz Drieb
Original Assignee
Basf Ag
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=39450917&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=CL2008000120(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Basf Ag filed Critical Basf Ag
Publication of CL2008000120A1 publication Critical patent/CL2008000120A1/es

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B17/00—Sulfur; Compounds thereof
    • C01B17/16—Hydrogen sulfides
    • C01B17/161—Preparation from elemental sulfur
    • C01B17/162—Preparation from elemental sulfur from elemental sulfur and hydrogen
    • 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
    • B01J10/00—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor
    • B01J10/005—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor carried out at high temperatures in the presence of a molten material
    • 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
    • B01J19/0053—Details of the reactor
    • 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
    • B01J19/2415—Tubular reactors
    • B01J19/242—Tubular reactors in series
    • 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
    • B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
    • 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
    • B01J8/06—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 in tube reactors; the solid particles being arranged in tubes
    • B01J8/067—Heating or cooling the reactor

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Catalysts (AREA)
  • Oxygen, Ozone, And Oxides In General (AREA)
CL200800120A 2007-01-16 2008-01-15 Reactor; y proceso para la preparacion continua de h2s por conversion de una mezcla reactante que contiene azufre gaseoso e hidrogeno sobre un catalizador y azufre fundido en la parte inferior del reactor que comprende que dicho catalizador esta disp CL2008000120A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP07100589 2007-01-16

Publications (1)

Publication Number Publication Date
CL2008000120A1 true CL2008000120A1 (es) 2008-05-23

Family

ID=39450917

Family Applications (1)

Application Number Title Priority Date Filing Date
CL200800120A CL2008000120A1 (es) 2007-01-16 2008-01-15 Reactor; y proceso para la preparacion continua de h2s por conversion de una mezcla reactante que contiene azufre gaseoso e hidrogeno sobre un catalizador y azufre fundido en la parte inferior del reactor que comprende que dicho catalizador esta disp

Country Status (15)

Country Link
US (1) US8021624B2 (es)
EP (1) EP2125612B1 (es)
JP (1) JP5306231B2 (es)
CN (1) CN101583564B (es)
AT (1) ATE503720T1 (es)
CA (1) CA2675506C (es)
CL (1) CL2008000120A1 (es)
DE (1) DE502008003008D1 (es)
DK (1) DK2125612T3 (es)
ES (1) ES2362155T3 (es)
PE (1) PE20081326A1 (es)
PL (1) PL2125612T3 (es)
PT (1) PT2125612E (es)
SI (1) SI2125612T1 (es)
WO (1) WO2008087110A1 (es)

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2612956T3 (es) * 2007-01-16 2017-05-19 Basf Se Reactor y procedimiento para la producción de ácido sulfhídrico
WO2012045349A1 (de) * 2010-10-06 2012-04-12 Silicon Fire Ag Verfahren und anlage zur synthese von kohlenwasserstoff
EP2676928A1 (de) 2012-06-22 2013-12-25 Evonik Industries AG Reaktor und Verfahren zur Herstellung von Schwefelwasserstoff
EP2676927A1 (de) 2012-06-22 2013-12-25 Evonik Industries AG Reaktor und Verfahren zur Herstellung von Schwefelwasserstoff
EP2676926A1 (de) 2012-06-22 2013-12-25 Evonik Industries AG Reaktor und Verfahren zur Herstellung von Schwefelwasserstoff
EP2676925A1 (de) 2012-06-22 2013-12-25 Evonik Industries AG Reaktor und Verfahren zur Herstellung von Schwefelwasserstoff
CN103272538A (zh) * 2013-04-26 2013-09-04 中昊光明化工研究设计院有限公司 液埋气室式反应塔
CN109277054B (zh) * 2018-11-15 2023-09-12 山东诺为制药流体系统有限公司 一种可进行淬灭的精确进料连续流反应系统
CN111252741B (zh) * 2019-12-27 2020-10-02 朱伯麟 一种工业合成硫化氢气体的稳态装置及方法
CN112221435A (zh) * 2020-09-27 2021-01-15 山东新和成氨基酸有限公司 一种连续制备硫化氢的反应器及方法
KR102692857B1 (ko) * 2022-01-24 2024-08-07 주식회사 레이크테크놀로지 황화수소 반응기

Family Cites Families (21)

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Publication number Priority date Publication date Assignee Title
NL26828C (es) * 1927-01-19
US1700578A (en) * 1927-05-05 1929-01-29 Raymond F Bacon Production of hydrogen sulphide
GB598885A (en) * 1939-05-11 1948-03-01 Pingris & Mollet Fontaine Reun Chemical reaction furnace with high thermal efficiency
US2474066A (en) * 1946-01-04 1949-06-21 Barium Reduction Corp Method of making hydrogen sulfide
US2687948A (en) * 1949-02-11 1954-08-31 Gregory Paul Methods of and means for thermal operations
US2965455A (en) * 1953-04-24 1960-12-20 Hooker Chemical Corp Apparatus for producing hydrogen sulfide
US2863725A (en) 1953-04-24 1958-12-09 Hooker Chemical Corp Process for making sulfur free hydrogen sulfide
DE1113446B (de) * 1960-06-09 1961-09-07 Basf Ag Verfahren zur Herstellung von Schwefelwasserstoff
US3672847A (en) * 1970-03-05 1972-06-27 Selas Corp Of America Reformer furnace
US3779711A (en) * 1971-07-19 1973-12-18 V Gryaznov Catalytic reactor designed for carrying out conjugate chemical reactions
US3851049A (en) * 1972-06-14 1974-11-26 Continental Oil Co Method for preparing hydrogen sulfide
US4233269A (en) 1978-11-09 1980-11-11 Exxon Research & Engineering Co. Gas liquid distributor
JPS63197534A (ja) * 1987-02-10 1988-08-16 Mitsubishi Heavy Ind Ltd 反応装置
JPH01257109A (ja) * 1988-04-07 1989-10-13 Jgc Corp 硫化水素の製造方法
JPH03103311A (ja) * 1989-09-14 1991-04-30 Jgc Corp 硫化水素の製造方法およびその製造装置
NL1008573C2 (nl) * 1998-03-12 1999-09-14 Dsm Nv Inrichting voor het uitvoeren van gas/vloeistof contact.
IT1299000B1 (it) * 1998-04-01 2000-02-07 Siirtec Nigi S P A Dispositivo e procedimento per migliorare la conversione in urea nella reazione fra anidride carbonica e ammoniaca
CN1569618A (zh) * 2004-05-12 2005-01-26 唐培堃 生产硫化氢的方法
US20060147357A1 (en) * 2004-12-31 2006-07-06 Nextgen Chemical Processes Inc. Thin film tube reactor
JP5393483B2 (ja) * 2007-01-16 2014-01-22 ビーエーエスエフ ソシエタス・ヨーロピア 硫化水素を連続的に製造するための方法および装置
WO2008087125A1 (de) * 2007-01-16 2008-07-24 Basf Se Verfahren und vorrichtung zur kontinuierlichen herstellung von schwefelwasserstoff

Also Published As

Publication number Publication date
JP2010515659A (ja) 2010-05-13
JP5306231B2 (ja) 2013-10-02
ES2362155T3 (es) 2011-06-29
DK2125612T3 (da) 2011-07-25
CA2675506C (en) 2016-07-19
EP2125612A1 (de) 2009-12-02
PT2125612E (pt) 2011-05-25
CN101583564A (zh) 2009-11-18
EP2125612B1 (de) 2011-03-30
US20100068128A1 (en) 2010-03-18
PE20081326A1 (es) 2008-11-12
ATE503720T1 (de) 2011-04-15
SI2125612T1 (sl) 2011-05-31
PL2125612T3 (pl) 2011-09-30
CA2675506A1 (en) 2008-07-24
US8021624B2 (en) 2011-09-20
DE502008003008D1 (de) 2011-05-12
WO2008087110A1 (de) 2008-07-24
CN101583564B (zh) 2012-07-04

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