MX2017011401A - Proceso para remover compuestos de azufre a partir de un gas con hidrogenacion y etapas de oxidacion directa. - Google Patents
Proceso para remover compuestos de azufre a partir de un gas con hidrogenacion y etapas de oxidacion directa.Info
- Publication number
- MX2017011401A MX2017011401A MX2017011401A MX2017011401A MX2017011401A MX 2017011401 A MX2017011401 A MX 2017011401A MX 2017011401 A MX2017011401 A MX 2017011401A MX 2017011401 A MX2017011401 A MX 2017011401A MX 2017011401 A MX2017011401 A MX 2017011401A
- Authority
- MX
- Mexico
- Prior art keywords
- hydrogenation
- gas
- sulfur
- catalyst
- direct oxidation
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8603—Removing sulfur compounds
- B01D53/8612—Hydrogen sulfide
- B01D53/8615—Mixtures of hydrogen sulfide and sulfur oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8603—Removing sulfur compounds
- B01D53/8612—Hydrogen sulfide
-
- 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
- C01B17/02—Preparation of sulfur; Purification
- C01B17/04—Preparation of sulfur; Purification from gaseous sulfur compounds including gaseous sulfides
- C01B17/0404—Preparation of sulfur; Purification from gaseous sulfur compounds including gaseous sulfides by processes comprising a dry catalytic conversion of hydrogen sulfide-containing gases, e.g. the Claus process
- C01B17/0426—Preparation of sulfur; Purification from gaseous sulfur compounds including gaseous sulfides by processes comprising a dry catalytic conversion of hydrogen sulfide-containing gases, e.g. the Claus process characterised by the catalytic conversion
- C01B17/0439—Preparation of sulfur; Purification from gaseous sulfur compounds including gaseous sulfides by processes comprising a dry catalytic conversion of hydrogen sulfide-containing gases, e.g. the Claus process characterised by the catalytic conversion at least one catalyst bed operating below the dew-point of sulfur
-
- 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
- C01B17/02—Preparation of sulfur; Purification
- C01B17/04—Preparation of sulfur; Purification from gaseous sulfur compounds including gaseous sulfides
- C01B17/0404—Preparation of sulfur; Purification from gaseous sulfur compounds including gaseous sulfides by processes comprising a dry catalytic conversion of hydrogen sulfide-containing gases, e.g. the Claus process
- C01B17/046—Preparation of sulfur; Purification from gaseous sulfur compounds including gaseous sulfides by processes comprising a dry catalytic conversion of hydrogen sulfide-containing gases, e.g. the Claus process without intermediate formation of sulfur dioxide
- C01B17/0469—Preparation of sulfur; Purification from gaseous sulfur compounds including gaseous sulfides by processes comprising a dry catalytic conversion of hydrogen sulfide-containing gases, e.g. the Claus process without intermediate formation of sulfur dioxide at least one catalyst bed operating below the dew-point of sulfur
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/207—Transition metals
- B01D2255/20707—Titanium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/207—Transition metals
- B01D2255/20738—Iron
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/207—Transition metals
- B01D2255/20746—Cobalt
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/207—Transition metals
- B01D2255/20753—Nickel
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/207—Transition metals
- B01D2255/20761—Copper
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/207—Transition metals
- B01D2255/20769—Molybdenum
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/207—Transition metals
- B01D2255/20776—Tungsten
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/207—Transition metals
- B01D2255/20784—Chromium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/209—Other metals
- B01D2255/2092—Aluminium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/65—Catalysts not containing noble metals
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/70—Non-metallic catalysts, additives or dopants
- B01D2255/702—Carbon
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/90—Physical characteristics of catalysts
- B01D2255/903—Multi-zoned catalysts
- B01D2255/9032—Two zones
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/90—Physical characteristics of catalysts
- B01D2255/904—Multiple catalysts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/30—Sulfur compounds
- B01D2257/306—Organic sulfur compounds, e.g. mercaptans
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/30—Sulfur compounds
- B01D2257/308—Carbonoxysulfide COS
-
- 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
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/584—Recycling of catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Biomedical Technology (AREA)
- Health & Medical Sciences (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Catalysts (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
La presente invención se refiere a un proceso para la remoción de azufre a partir de un gas que contiene compuestos de azufre como H2S, SO2, COS, CS2..., en una cantidad de hasta 15% en peso; en particular se refiere a gases que se emanan del proceso Claus. El proceso comprende una primera hidrogenación de componentes de azufre en H2S, el gas de hidrogenación es usado para regenerar un lecho desactivado de catalizador de oxidación, ambos se llevan a cabo a 200-500 °C. Después de la remoción de azufre, el gas resultante se somete a una segunda etapa de hidrogenación y después a una etapa de oxidación directa, tal etapa es operada por debajo del punto de rocío del azufre para atrapar el azufre formado en el catalizador. En el ciclo adicional, las corrientes de gas son intercambiadas para así regenerar el catalizador en la corrida el cual es desactivado. En una modalidad preferida, el proceso opera en al menos 2 reactores idénticos, cada uno contiene un lecho de catalizador de hidrogenación al que le sigue (en el sentido del flujo de gas) un lecho catalizador de oxidación directa que contiene un intercambiador de calor integrado.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP15158886.0A EP3067109B1 (en) | 2015-03-12 | 2015-03-12 | Process for removing sulfur compounds from a gas with hydrogenation and direct oxidation steps |
| PCT/EP2016/055323 WO2016142528A1 (en) | 2015-03-12 | 2016-03-11 | Process for removing sulfur compounds from a gas with hydrogenation and direct oxidation steps |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| MX2017011401A true MX2017011401A (es) | 2017-12-20 |
Family
ID=52810944
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| MX2017011401A MX2017011401A (es) | 2015-03-12 | 2016-03-11 | Proceso para remover compuestos de azufre a partir de un gas con hidrogenacion y etapas de oxidacion directa. |
Country Status (12)
| Country | Link |
|---|---|
| US (1) | US9586177B2 (es) |
| EP (1) | EP3067109B1 (es) |
| JP (1) | JP2018510777A (es) |
| CN (1) | CN107531481B (es) |
| AU (1) | AU2016231057A1 (es) |
| BR (1) | BR112017018578A2 (es) |
| CA (1) | CA2977451C (es) |
| ES (1) | ES2711612T3 (es) |
| MX (1) | MX2017011401A (es) |
| RU (1) | RU2703247C2 (es) |
| SA (1) | SA517382277B1 (es) |
| WO (1) | WO2016142528A1 (es) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107441875A (zh) * | 2017-09-08 | 2017-12-08 | 中冶焦耐(大连)工程技术有限公司 | 一种克劳斯尾气冷凝处理装置 |
| CN110937648B (zh) | 2019-12-25 | 2021-03-30 | 浙江工业大学 | 一种连续化处理高浓度有机废水的工艺及装置 |
| CN112014261B (zh) * | 2020-09-04 | 2022-04-26 | 西南石油大学 | 一种基于溶剂溶解原理测量吸附硫含量的装置及方法 |
Family Cites Families (25)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1900751A (en) * | 1928-02-27 | 1933-03-07 | Ig Farbenindustrie Ag | Purification of gases |
| US2758913A (en) * | 1951-10-11 | 1956-08-14 | Stanolind Oil & Gas Co | Process for sulfur recovery |
| NL171144B (nl) * | 1970-07-17 | 1982-09-16 | Shell Int Research | Werkwijze voor het verlagen van het totale zwavelgehalte van clausafgassen. |
| DE2501557A1 (de) * | 1975-01-16 | 1976-07-22 | Metallgesellschaft Ag | Verfahren und vorrichtung zur gewinnung von elementarem schwefel |
| US4035474A (en) * | 1976-03-01 | 1977-07-12 | Standard Oil Company (Indiana) | CBA for Claus tail gas cleanup |
| DE2755138C3 (de) * | 1977-12-10 | 1980-08-28 | Davy International Ag, 6000 Frankfurt | Verfahren zur Umsetzung eines Schwefeldioxid und Schwefelwasserstoff enthaltenden Gases unter Bildung von elementarem Schwefel |
| FR2481254A1 (fr) * | 1980-04-23 | 1981-10-30 | Elf Aquitaine | Procede pour l'incineration catalytique de gaz residuaires renfermant en faible concentration au moins un compose du soufre choisi parmi cos, cs2, et les mercaptans et eventuellement au moins un membre du groupe forme par h2s, so2, soufre vapeur et/ou vesiculaire |
| US4507275A (en) * | 1983-08-30 | 1985-03-26 | Standard Oil Company (Indiana) | Process for producing and recovering elemental sulfur from acid gas |
| DE3526706A1 (de) * | 1985-07-25 | 1987-01-29 | Linde Ag | Verfahren und reaktor zur katalytischen umsetzung von schwefelwasserstoff zu elementarem schwefel |
| US5202107A (en) * | 1988-06-08 | 1993-04-13 | Societe National Elf Aquitaine (Prod.) | Process for improving the sulphur yield of a complex for the production of sulphur followed by a purification unit |
| FR2702674B1 (fr) * | 1993-03-16 | 1995-04-28 | Elf Aquitaine | Procédé d'élimination des composés soufrés contenus dans un gaz résiduaire du type gaz résiduaire d'usine à soufre Claus, avec récupération desdits composés sous la forme de soufre. |
| FR2702673B1 (fr) * | 1993-03-16 | 1995-04-28 | Elf Aquitaine | Procédé d'élimination de l'H2S contenu dans un gaz en concentration inférieure à 5 % en volume avec récupération de cet H2S sous la forme de soufre. |
| DE4409203A1 (de) * | 1994-03-17 | 1995-09-21 | Linde Ag | Verfahren zur Gewinnung von elementarem Schwefel aus einem H¶2¶S enthaltenden Gasgemisch |
| FR2740704B1 (fr) * | 1995-11-03 | 1997-12-26 | Elf Aquitaine | Procede d'elimination quasi totale des composes soufres h2s, so2, cos et/ou cs2 contenus dans un gaz residuaire d'usine a soufre, avec recuperation desdits composes sous la forme de soufre |
| FR2740703B1 (fr) * | 1995-11-03 | 1997-12-05 | Elf Aquitaine | Procede d'elimination quasi totale des composes soufres h2s, so2, cos et/ou cs2 contenus dans un gaz residuaire d'usine a soufre, avec recuperation desdits composes sous la forme de soufre |
| FR2740767B1 (fr) * | 1995-11-03 | 1997-12-26 | Elf Aquitaine | Procede d'oxydation complete en soufre de l'h2s present dans un gaz et son application a la recuperation quasi totale, sous la forme de soufre, des composes soufres contenus dans un gaz residuaire d'usine a soufre |
| FR2762592B1 (fr) | 1997-04-24 | 1999-06-18 | Elf Aquitaine | Procede d'elimination des composes soufres h2s, so2, cos et/ou cs2 contenus dans un gaz residuaire d'usine a soufre avec recuperation desdits composes sous la forme de soufre |
| DE19719375A1 (de) | 1997-05-07 | 1998-11-12 | Linde Ag | Verfahren und Reaktor zur Herstellung von Ethylenoxid |
| DE19754185C1 (de) | 1997-12-06 | 1999-02-04 | Deg Engineering Gmbh | Reaktor für die katalytische Umsetzung von Reaktionsmedien, insbesondere von gasförmigen Reaktionsmedien |
| EP1737788A4 (en) * | 2004-04-22 | 2011-10-26 | Fluor Tech Corp | IMPROVED CONFIGURATIONS AND PROCESSES FOR EXHAUST TREATMENT |
| DE102005022164B4 (de) * | 2005-05-13 | 2009-08-06 | Lurgi Gmbh | Vorrichtung und Verfahren zum Betrieb der Vorrichtung zur kontinuierlichen Rückgewinnung von Schwefel aus H2S enthaltendem Gas |
| EP1902769A1 (en) * | 2006-09-22 | 2008-03-26 | Jacobs Nederland B.V. | Process for the recovery of sulfur from sulfur containing gases |
| WO2009111585A1 (en) * | 2008-03-04 | 2009-09-11 | Worleyparsons Group, Inc. | Process for catalytic tail gas incineration |
| PL2594328T3 (pl) | 2011-11-21 | 2014-12-31 | Its Reaktortechnik Gmbh | Proces do usuwania siarkowodoru ze strumienia gazu |
| US8703084B2 (en) | 2012-02-17 | 2014-04-22 | Archon Technologies Ltd. | Removal of sulfur compounds from a gas stream |
-
2015
- 2015-03-12 EP EP15158886.0A patent/EP3067109B1/en active Active
- 2015-03-12 ES ES15158886T patent/ES2711612T3/es active Active
- 2015-04-16 US US14/688,067 patent/US9586177B2/en active Active
-
2016
- 2016-03-11 AU AU2016231057A patent/AU2016231057A1/en not_active Abandoned
- 2016-03-11 BR BR112017018578A patent/BR112017018578A2/pt not_active Application Discontinuation
- 2016-03-11 WO PCT/EP2016/055323 patent/WO2016142528A1/en not_active Ceased
- 2016-03-11 CN CN201680015041.5A patent/CN107531481B/zh active Active
- 2016-03-11 CA CA2977451A patent/CA2977451C/en active Active
- 2016-03-11 JP JP2017566205A patent/JP2018510777A/ja not_active Ceased
- 2016-03-11 MX MX2017011401A patent/MX2017011401A/es unknown
- 2016-03-11 RU RU2017134117A patent/RU2703247C2/ru active
-
2017
- 2017-09-11 SA SA517382277A patent/SA517382277B1/ar unknown
Also Published As
| Publication number | Publication date |
|---|---|
| RU2017134117A3 (es) | 2019-05-14 |
| CA2977451C (en) | 2022-12-13 |
| US9586177B2 (en) | 2017-03-07 |
| US20160263524A1 (en) | 2016-09-15 |
| ES2711612T3 (es) | 2019-05-06 |
| SA517382277B1 (ar) | 2022-06-26 |
| EP3067109A1 (en) | 2016-09-14 |
| BR112017018578A2 (pt) | 2018-04-24 |
| CN107531481A (zh) | 2018-01-02 |
| JP2018510777A (ja) | 2018-04-19 |
| EP3067109B1 (en) | 2018-12-05 |
| AU2016231057A1 (en) | 2017-09-14 |
| CN107531481B (zh) | 2020-09-15 |
| CA2977451A1 (en) | 2016-09-15 |
| RU2017134117A (ru) | 2019-04-03 |
| RU2703247C2 (ru) | 2019-10-15 |
| WO2016142528A1 (en) | 2016-09-15 |
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