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PE20081326A1 - Reactor y proceso para preparar sulfuro de hidrogeno - Google Patents

Reactor y proceso para preparar sulfuro de hidrogeno

Info

Publication number
PE20081326A1
PE20081326A1 PE2008000140A PE2008000140A PE20081326A1 PE 20081326 A1 PE20081326 A1 PE 20081326A1 PE 2008000140 A PE2008000140 A PE 2008000140A PE 2008000140 A PE2008000140 A PE 2008000140A PE 20081326 A1 PE20081326 A1 PE 20081326A1
Authority
PE
Peru
Prior art keywords
reactor
shaped tube
catalyst
reactant mixture
region
Prior art date
Application number
PE2008000140A
Other languages
English (en)
Inventor
Andreas Wolfert
Harald Jachow
Heinz Driess
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=PE20081326(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 PE20081326A1 publication Critical patent/PE20081326A1/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)

Abstract

DONDE EL REACTOR INCLUYE: i)UN DISPOSITIVO DISTRIBUIDOR PARA ALIMENTAR HIDROGENO GASEOSO, QUE COMPRENDE UNA PLACA DISTRIBUIDORA CON UN BORDE QUE SE EXTIENDE EN DIRECCION DESCENDENTE PARA FORMAR UNA BURBUJA DE HIDROGENO; ii)AL MENOS UN TUBO EN FORMA DE U, DONDE SE DISPONE EL CATALIZADOR, QUE TIENE AL MENOS UN ORIFICIO DE ENTRADA EN UNA RAMA DISPUESTA SOBRE LA FUNDICION DE AZUFRE Y TIENE AL MENOS UN ORIFICIO DE SALIDA EN OTRA RAMA A TRAVES DEL CUAL SALE UN PRODUCTO A UNA REGION DE PRODUCTO; Y, iii)UNA REGION DE REACTIVOS QUE TIENE UNA MEZCLA REACTIVA QUE CONTIENE AZUFRE E HIDROGENO GASEOSOS SOBRE UN CATALIZADOR. (ii) ESTA MONTADO SOBRE UNA PLACA QUE ESTA DISPUESTA EN UNA PARTE SUPERIOR DEL REACTOR Y ESTA CONECTADA A UNA CAMISA DEL REACTOR. UN LECHO INERTE SE DISPONE CORRIENTE ARRIBA DEL CATALIZADOR EN DIRECCION DEL FLUJO DE LA MEZCLA REACTIVA EN (ii). EL PROCESO COMPRENDE: a)PROVEER UNA FUNDICION DE AZUFRE AL MENOS EN LA PARTE INFERIOR DEL REACTOR, EN LA CUAL SE INTRODUCE HIDROGENO GASEOSO; b)INTRODUCIR LA MEZCLA REACTIVA DESDE (iii) HACIA UNA RAMA DE (ii) A TRAVES DE AL MENOS UN ORIFICIO DE ENTRADA DISPUESTO SOBRE DICHA FUNDICION; c)PASAR LA MEZCLA REACTIVA A LO LARGO DE LA VIA DE FLUJO A TRAVES DE (ii), QUE ESTA EN PARTE EN CONTACTO CON DICHA FUNDICION, CONVIRTIENDOSE LA MEZCLA REACTIVA SOBRE UN CATALIZADOR DISPUESTO EN LA VIA DE FLUJO EN UNA REGION DE REACCION; Y, d)PASAR UN PRODUCTO A TRAVES DE AL MENOS UN ORIFICIO DE SALIDA EN OTRA RAMA DE (ii) A UNA REGION DE PRODUCTO
PE2008000140A 2007-01-16 2008-01-15 Reactor y proceso para preparar sulfuro de hidrogeno PE20081326A1 (es)

Applications Claiming Priority (1)

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

Publications (1)

Publication Number Publication Date
PE20081326A1 true PE20081326A1 (es) 2008-11-12

Family

ID=39450917

Family Applications (1)

Application Number Title Priority Date Filing Date
PE2008000140A PE20081326A1 (es) 2007-01-16 2008-01-15 Reactor y proceso para preparar sulfuro de hidrogeno

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
CN101610976B (zh) * 2007-01-16 2012-12-05 巴斯夫欧洲公司 生产硫化氢的反应器和方法
EP2624947B1 (de) * 2010-10-06 2016-04-27 Silicon Fire AG Verfahren und anlage zur synthese von kohlenwasserstoff
EP2676925A1 (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
EP2676928A1 (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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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
WO2007075174A2 (en) * 2004-12-31 2007-07-05 Nextgen Chemical Processes Inc. Thin film tube reactor
PL2460584T3 (pl) * 2007-01-16 2016-09-30 Urządzenie do ciągłego wytwarzania siarkowodoru
ES2612303T3 (es) * 2007-01-16 2017-05-16 Basf Se Método y dispositivo para la producción continua de sulfuro de hidrógeno

Also Published As

Publication number Publication date
CL2008000120A1 (es) 2008-05-23
CN101583564A (zh) 2009-11-18
ES2362155T3 (es) 2011-06-29
CA2675506A1 (en) 2008-07-24
EP2125612B1 (de) 2011-03-30
DK2125612T3 (da) 2011-07-25
CN101583564B (zh) 2012-07-04
DE502008003008D1 (de) 2011-05-12
SI2125612T1 (sl) 2011-05-31
JP2010515659A (ja) 2010-05-13
EP2125612A1 (de) 2009-12-02
JP5306231B2 (ja) 2013-10-02
WO2008087110A1 (de) 2008-07-24
CA2675506C (en) 2016-07-19
ATE503720T1 (de) 2011-04-15
US20100068128A1 (en) 2010-03-18
PL2125612T3 (pl) 2011-09-30
US8021624B2 (en) 2011-09-20
PT2125612E (pt) 2011-05-25

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