DK2225035T3 - Fremgangsmåde til katalysatorgenindvinding - Google Patents
Fremgangsmåde til katalysatorgenindvinding Download PDFInfo
- Publication number
- DK2225035T3 DK2225035T3 DK08859059.1T DK08859059T DK2225035T3 DK 2225035 T3 DK2225035 T3 DK 2225035T3 DK 08859059 T DK08859059 T DK 08859059T DK 2225035 T3 DK2225035 T3 DK 2225035T3
- Authority
- DK
- Denmark
- Prior art keywords
- acid
- extractant
- process according
- spent catalyst
- catalyst
- Prior art date
Links
Classifications
-
- 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
- B01J38/00—Regeneration or reactivation of catalysts, in general
- B01J38/48—Liquid treating or treating in liquid phase, e.g. dissolved or suspended
- B01J38/68—Liquid treating or treating in liquid phase, e.g. dissolved or suspended including substantial dissolution or chemical precipitation of a catalyst component in the ultimate reconstitution of the catalyst
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/24—Chromium, molybdenum or tungsten
- B01J23/30—Tungsten
-
- 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
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/14—Phosphorus; Compounds thereof
- B01J27/186—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J27/188—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
-
- 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
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/28—Regeneration or reactivation
- B01J27/285—Regeneration or reactivation of catalysts comprising compounds of phosphorus
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/40—Catalysts, in general, characterised by their form or physical properties characterised by dimensions, e.g. grain size
-
- 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
- B01J38/00—Regeneration or reactivation of catalysts, in general
- B01J38/74—Regeneration or reactivation of catalysts, in general utilising ion-exchange
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
- C07C1/20—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms
- C07C1/24—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms by elimination of water
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B34/00—Obtaining refractory metals
- C22B34/30—Obtaining chromium, molybdenum or tungsten
- C22B34/36—Obtaining tungsten
- C22B34/365—Obtaining tungsten from spent catalysts
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/90—Regeneration or reactivation
- B01J23/92—Regeneration or reactivation of catalysts comprising metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
- B01J35/34—Mechanical properties
- B01J35/37—Crush or impact strength
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/615—100-500 m2/g
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/64—Pore diameter
- B01J35/647—2-50 nm
-
- 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
- B01J38/00—Regeneration or reactivation of catalysts, in general
- B01J38/04—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst
- B01J38/06—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst using steam
-
- 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
- B01J38/00—Regeneration or reactivation of catalysts, in general
- B01J38/48—Liquid treating or treating in liquid phase, e.g. dissolved or suspended
- B01J38/50—Liquid treating or treating in liquid phase, e.g. dissolved or suspended using organic liquids
- B01J38/52—Liquid treating or treating in liquid phase, e.g. dissolved or suspended using organic liquids oxygen-containing
-
- 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
- B01J38/00—Regeneration or reactivation of catalysts, in general
- B01J38/48—Liquid treating or treating in liquid phase, e.g. dissolved or suspended
- B01J38/50—Liquid treating or treating in liquid phase, e.g. dissolved or suspended using organic liquids
- B01J38/56—Hydrocarbons
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- C07C2523/24—Chromium, molybdenum or tungsten
- C07C2523/30—Tungsten
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2527/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- C07C2527/14—Phosphorus; Compounds thereof
- C07C2527/16—Phosphorus; Compounds thereof containing oxygen
- C07C2527/18—Phosphorus; Compounds thereof containing oxygen with metals
-
- 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
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
-
- 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
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
-
- 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)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Manufacturing & Machinery (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Claims (10)
1. Fremgangsmåde til genindvinding af heteropolywolframsyre fra en brugt katalysator omfattende en understøttet heteropolywolframsyre kendetegnet ved, at fremgangsmåden omfatter: (a) at bringe den brugte katalysator i kontakt med et ekstraktionsmiddel udvalgt blandt vand, methanol, ethanol eller en blanding af hvilke som helst to eller flere deraf i et tidsrum, der er tilstrækkeligt til at ekstrahere mindst en del af heteropolywolframsyren derfra; (b) at fraseparere ekstraktionsmidlet indeholdende heteropolywolframsyre fra den behandlede brugte katalysator; (c) at bringe ekstraktionsmidlet indeholdende heteropolywolframsyre i kontakt med en kraftig ionvekslingsresin for at tjerne nikkel, kobolt, chrom og jern, som er blevet udvasket fra den brugte katalysator i trin (a) indeholdt deri og (d) at genindvinde det behandlede ekstraktionsmiddel indeholdende heteropolywolframsyre til efterfølgende brug.
2. Fremgangsmåde ifølge krav 1, hvor heteropolysyren er wolframsiliciumsyre eller wolframphosphorsyre.
3. Fremgangsmåde ifølge krav 1 eller krav 2, kendetegnet ved, at den brugte katalysator vaskes inden trin (a) med en organisk væske for at fjerne blød koks.
4. Fremgangsmåde ifølge krav 1 kendetegnet ved, at trin (a) udføres ved en temperatur i området fra 40° til 85°C.
5. Fremgangsmåde ifølge krav 1 kendetegnet ved, at ekstraktionsmidlet er en blanding af ethanol og vand.
6. Fremgangsmåde ifølge krav 1 kendetegnet ved, at ekstraktionsmidlet er vand.
7. Fremgangsmåde ifølge krav 1 kendetegnet ved, at ekstraktionsmidlet er ethanol, og at der forud for trin (c) går et trin, hvor blød koks opløst i ekstraktionsmidlet fjernes under anvendelse af væske-væskeekstraktion.
8. Fremgangsmåde ifølge krav 1 kendetegnet ved, at den brugte katalysator er blevet anvendt til at bevirke dehydreringen af ethoxyethan, ethanol eller blandinger deraf for at danne ethen.
9. Fremgangsmåde ifølge krav 1 kendetegnet ved, at genindvundet hetero-polywolframsyre genbruges til fremstilling af frisk understøttet heteropolywol-framsyre.
10. Fremgangsmåde ifølge krav 3 kendetegnet ved, at den organiske væske er en C6- til Cio-alkan eller en blanding deraf.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP07254848A EP2075070A1 (en) | 2007-12-13 | 2007-12-13 | Catalyst recovery process |
| PCT/GB2008/004014 WO2009074774A2 (en) | 2007-12-13 | 2008-12-03 | Catalyst recovery process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DK2225035T3 true DK2225035T3 (da) | 2018-06-18 |
Family
ID=39507445
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DK08859059.1T DK2225035T3 (da) | 2007-12-13 | 2008-12-03 | Fremgangsmåde til katalysatorgenindvinding |
Country Status (11)
| Country | Link |
|---|---|
| US (1) | US20100210448A1 (da) |
| EP (2) | EP2075070A1 (da) |
| CN (1) | CN101896269B (da) |
| AR (1) | AR072762A1 (da) |
| BR (1) | BRPI0819848A2 (da) |
| DK (1) | DK2225035T3 (da) |
| ES (1) | ES2671451T3 (da) |
| RU (1) | RU2484900C2 (da) |
| TR (1) | TR201807479T4 (da) |
| WO (1) | WO2009074774A2 (da) |
| ZA (1) | ZA201002129B (da) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP2287145A1 (en) | 2009-08-12 | 2011-02-23 | BP p.l.c. | Process for purifying ethylene |
| US11338280B2 (en) * | 2020-02-03 | 2022-05-24 | Usa Debusk Llc | Catalytic reactor system treatment processes |
Family Cites Families (22)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2968527A (en) * | 1957-10-03 | 1961-01-17 | Columbia Southern Chem Corp | Method of recovering tungstic acid values from aqueous media |
| GB894592A (en) * | 1957-10-03 | 1962-04-26 | Columbia Southern Chem Corp | Process for the recovery of tungstic acid catalyst |
| US3644497A (en) * | 1968-11-01 | 1972-02-22 | Celanese Corp | Conversion of ethylenically unsaturated compounds using heteropoly-molybdic and heteropolytungstic acids as catalysts |
| GB1518338A (en) * | 1974-11-18 | 1978-07-19 | Degussa | Process for separating epoxidation and hydroxylation catalysts from distillation residues |
| US4007130A (en) * | 1975-12-29 | 1977-02-08 | Monsanto Company | Catalyst regeneration method |
| CA1150293A (en) * | 1979-10-01 | 1983-07-19 | Keisuke Wada | Process for the production of methylenedicarbanilates |
| JPS56163755A (en) * | 1980-05-23 | 1981-12-16 | Mitsubishi Chem Ind Ltd | Recovery method for heteropolyacid catalyst component |
| US5716895A (en) * | 1993-04-01 | 1998-02-10 | Nippon Kayaku Kabushiki Kaisha | Process for regeneration of catalysts |
| US5387702A (en) | 1993-09-29 | 1995-02-07 | Council Of Scientific And Industrial Research | Process for the preparation of cabofuran |
| CN1093000C (zh) * | 1996-12-27 | 2002-10-23 | 吉林化学工业公司研究院 | 醚裂解制异丁烯催化剂及其应用 |
| JP3887511B2 (ja) * | 1999-05-19 | 2007-02-28 | 三菱レイヨン株式会社 | 触媒の製造方法 |
| EP1172348A1 (en) | 2000-07-14 | 2002-01-16 | Haldor Topsoe A/S | Process of paraffin isomerisation |
| GB0113079D0 (en) * | 2001-05-30 | 2001-07-18 | Kvaerner Process Tech Ltd | Process |
| GB0316756D0 (en) * | 2003-07-17 | 2003-08-20 | Bp Chem Int Ltd | Process |
| JP4764338B2 (ja) * | 2004-02-24 | 2011-08-31 | 三菱レイヨン株式会社 | モリブデンの回収方法及び触媒の製造方法 |
| US7291272B2 (en) * | 2004-05-07 | 2007-11-06 | Orica Australia Pty Ltd. | Inorganic contaminant removal from water |
| GB0410289D0 (en) * | 2004-05-07 | 2004-06-09 | Bp Chem Int Ltd | Process |
| CN101253133B (zh) * | 2005-07-06 | 2012-06-06 | 英国石油化学品有限公司 | 用于混合醇脱水的反应蒸馏 |
| US7485267B2 (en) * | 2005-07-29 | 2009-02-03 | Chevron U.S.A. Inc. | Process for metals recovery from spent catalyst |
| EP1790627A1 (en) * | 2005-11-29 | 2007-05-30 | BP Chemicals Limited | Process for producing olefins |
| US20080053909A1 (en) * | 2006-09-06 | 2008-03-06 | Fassbender Alexander G | Ammonia recovery process |
| JP5172859B2 (ja) * | 2007-01-19 | 2013-03-27 | ザ・ピュロライト・カンパニー | 逆浸透膜の汚染減少 |
-
2007
- 2007-12-13 EP EP07254848A patent/EP2075070A1/en not_active Ceased
-
2008
- 2008-12-03 TR TR2018/07479T patent/TR201807479T4/tr unknown
- 2008-12-03 BR BRPI0819848-9A patent/BRPI0819848A2/pt not_active Application Discontinuation
- 2008-12-03 CN CN2008801203735A patent/CN101896269B/zh active Active
- 2008-12-03 US US12/733,811 patent/US20100210448A1/en not_active Abandoned
- 2008-12-03 DK DK08859059.1T patent/DK2225035T3/da active
- 2008-12-03 EP EP08859059.1A patent/EP2225035B1/en active Active
- 2008-12-03 ES ES08859059.1T patent/ES2671451T3/es active Active
- 2008-12-03 RU RU2010128238/04A patent/RU2484900C2/ru active
- 2008-12-03 WO PCT/GB2008/004014 patent/WO2009074774A2/en not_active Ceased
- 2008-12-12 AR ARP080105435A patent/AR072762A1/es unknown
-
2010
- 2010-03-25 ZA ZA2010/02129A patent/ZA201002129B/en unknown
Also Published As
| Publication number | Publication date |
|---|---|
| AR072762A1 (es) | 2010-09-22 |
| US20100210448A1 (en) | 2010-08-19 |
| ES2671451T3 (es) | 2018-06-06 |
| EP2225035A2 (en) | 2010-09-08 |
| CN101896269B (zh) | 2013-06-19 |
| ZA201002129B (en) | 2014-09-25 |
| WO2009074774A2 (en) | 2009-06-18 |
| EP2075070A1 (en) | 2009-07-01 |
| CN101896269A (zh) | 2010-11-24 |
| BRPI0819848A2 (pt) | 2015-06-16 |
| WO2009074774A3 (en) | 2009-11-05 |
| RU2010128238A (ru) | 2012-01-20 |
| RU2484900C2 (ru) | 2013-06-20 |
| EP2225035B1 (en) | 2018-04-25 |
| TR201807479T4 (tr) | 2018-06-21 |
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