WO2007118825A1 - Method and device for the controlled regeneration of a catalyst and a reactor - Google Patents
Method and device for the controlled regeneration of a catalyst and a reactor Download PDFInfo
- Publication number
- WO2007118825A1 WO2007118825A1 PCT/EP2007/053507 EP2007053507W WO2007118825A1 WO 2007118825 A1 WO2007118825 A1 WO 2007118825A1 EP 2007053507 W EP2007053507 W EP 2007053507W WO 2007118825 A1 WO2007118825 A1 WO 2007118825A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- burner
- catalyst
- reactor
- burners
- regeneration
- 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
- B01J38/02—Heat treatment
-
- 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
- B01J8/062—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 being installed in a furnace
-
- 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
- B01J38/12—Treating with free oxygen-containing gas
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C11/00—Aliphatic unsaturated hydrocarbons
- C07C11/02—Alkenes
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/32—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00504—Controlling the temperature by means of a burner
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00716—Means for reactor start-up
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00157—Controlling the temperature by means of a burner
-
- 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
-
- 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
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/90—Regeneration or reactivation
-
- 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
Definitions
- the invention relates to a process for the regeneration of a catalyst in a reactor, which is equipped with at least one burner, as well as a device for carrying out the method.
- the catalytic conversion of the hydrocarbon-containing feed into the desired olefin products proceeds under heat absorption (endothermic).
- endothermic In order to maintain the temperatures required for an endothermic catalytic reaction in a reactor, it is usually provided with one or more burners.
- the catalytic reaction usually by-products, such as. As carbon, which precipitate on the catalyst and disable it. For this reason, the catalyst has to be regenerated, for which the supply of starting materials is interrupted in a batch process and, for example, oxidizing gas is passed over the catalyst (see H. Bölt, F. Walser, Linde Reports on Science and Technology 49, 3-8 (1991)).
- the burners of the reactor are kept at minimum load (German Patent, DE 34 39 166). This can lead to the occurrence of temperature peaks, which can irreparably damage the catalyst. This leads to a reduction of the catalyst activity and thus to a reduction of the product yield in the catalysis cycle along with a reduction of the catalyst lifetime.
- This object is achieved in that the burners are turned off during the regeneration phase of the catalyst.
- the burners switched off are re-ignited after the regeneration phase via at least one pilot burner.
- the flame of the pilot burner and the burner is monitored.
- An adaptation of the heat output of the pilot burner to compensate for heat losses of the reactor is also appropriate.
- the deactivated burners are activated again by means of electronic ignition. On the device side, this object is achieved in that the burners have a shut-off device in the reactor.
- the reactor is expediently equipped with at least one pilot burner as well as with a pilot burner monitoring device and the burners.
- a means for controlling the performance of the pilot burner is also useful.
- the device contains a device for the electronic reignition of the burner.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Catalysts (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Hydrogen, Water And Hydrids (AREA)
Abstract
Description
Claims
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP07727975A EP2010313A1 (en) | 2006-04-18 | 2007-04-11 | Method and device for the controlled regeneration of a catalyst and a reactor |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102006017908.0 | 2006-04-18 | ||
DE102006017908A DE102006017908A1 (en) | 2006-04-18 | 2006-04-18 | Method and apparatus for controlled regeneration of a catalyst and reactor |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2007118825A1 true WO2007118825A1 (en) | 2007-10-25 |
Family
ID=38222699
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2007/053507 WO2007118825A1 (en) | 2006-04-18 | 2007-04-11 | Method and device for the controlled regeneration of a catalyst and a reactor |
Country Status (6)
Country | Link |
---|---|
EP (1) | EP2010313A1 (en) |
KR (1) | KR20080112345A (en) |
CN (1) | CN101426570A (en) |
DE (1) | DE102006017908A1 (en) |
RU (1) | RU2008145106A (en) |
WO (1) | WO2007118825A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102009012663B3 (en) * | 2009-03-13 | 2010-09-16 | Uhde Gmbh | Process and device for the uniform production of steam from the waste heat of an alkane dehydrogenation |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3087797A (en) * | 1961-04-24 | 1963-04-30 | Lummus Co | Regenerative furnace |
US4513162A (en) * | 1981-08-18 | 1985-04-23 | Davy Mckee Aktiengesellschaft | Dehydrogenation process |
US6191332B1 (en) * | 1991-05-06 | 2001-02-20 | Institut Francais Du Petrole | Method and apparatus for dehydrogenating aliphatic hydrocarbons to olefinic hydrocarbons |
WO2006060999A1 (en) * | 2004-12-10 | 2006-06-15 | Webasto Ag | Method for regenerating a reformer |
-
2006
- 2006-04-18 DE DE102006017908A patent/DE102006017908A1/en not_active Withdrawn
-
2007
- 2007-04-11 RU RU2008145106/15A patent/RU2008145106A/en not_active Application Discontinuation
- 2007-04-11 EP EP07727975A patent/EP2010313A1/en not_active Withdrawn
- 2007-04-11 CN CNA2007800138471A patent/CN101426570A/en active Pending
- 2007-04-11 WO PCT/EP2007/053507 patent/WO2007118825A1/en active Application Filing
- 2007-04-11 KR KR1020087026385A patent/KR20080112345A/en not_active Application Discontinuation
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3087797A (en) * | 1961-04-24 | 1963-04-30 | Lummus Co | Regenerative furnace |
US4513162A (en) * | 1981-08-18 | 1985-04-23 | Davy Mckee Aktiengesellschaft | Dehydrogenation process |
US6191332B1 (en) * | 1991-05-06 | 2001-02-20 | Institut Francais Du Petrole | Method and apparatus for dehydrogenating aliphatic hydrocarbons to olefinic hydrocarbons |
WO2006060999A1 (en) * | 2004-12-10 | 2006-06-15 | Webasto Ag | Method for regenerating a reformer |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102009012663B3 (en) * | 2009-03-13 | 2010-09-16 | Uhde Gmbh | Process and device for the uniform production of steam from the waste heat of an alkane dehydrogenation |
CN102348500A (en) * | 2009-03-13 | 2012-02-08 | 犹德有限公司 | Method and apparatus for a constant steam generation from the waste heat of an alkane dehydrogenation |
CN102348500B (en) * | 2009-03-13 | 2013-12-18 | 犹德有限公司 | Method and apparatus for constant steam generation from waste heat of alkane dehydrogenation |
Also Published As
Publication number | Publication date |
---|---|
EP2010313A1 (en) | 2009-01-07 |
CN101426570A (en) | 2009-05-06 |
DE102006017908A1 (en) | 2007-10-25 |
KR20080112345A (en) | 2008-12-24 |
RU2008145106A (en) | 2010-05-27 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Chen et al. | Catalytic hydroprocessing of fatty acid methyl esters to renewable alkane fuels over Ni/HZSM-5 catalyst | |
US8784645B2 (en) | Process for producing hydrocarbon oil | |
US8912374B2 (en) | Process for producing paraffinic hydrocarbons | |
JP5863878B2 (en) | Olefin production process | |
US20120216450A1 (en) | Method of converting feeds from renewable sources in co-processing with a petroleum feed using a catalyst based on nickel and molybdenum | |
DE202009019033U1 (en) | Energy recovery | |
US20110166405A1 (en) | Process for producing paraffinic hydrocarbons | |
EP3938337B1 (en) | Method and installation for the production of one or more olefins | |
EP2267102A1 (en) | System and method for manufacturing gas from a biomass gasification | |
CA2833204A1 (en) | Catalytic process and apparatus for producing hydrocarbons from biooils | |
Singh et al. | Hydrodesulfurization of dibenzothiophene on NiMo/γ-Al2O3 washcoated monoliths | |
WO2019233673A1 (en) | Method, tube bundle reactor and reactor system for carrying out catalytic gas phase reactions | |
JP6336081B2 (en) | A cocurrent adiabatic reaction system for converting raw materials rich in triacylglycerol | |
WO2007118825A1 (en) | Method and device for the controlled regeneration of a catalyst and a reactor | |
CN102041047B (en) | Heavy oil hydrogenation modifying method | |
DE102014007001A1 (en) | Process and plant for the production of H2-rich synthesis gas | |
EP2756055B1 (en) | Renewable diesel refinery strategy | |
EP2739386B1 (en) | Method for carrying out catalytic autothermal gas phase dehydrogenation in production and regeneration modes | |
EP2595944B1 (en) | Method for producing acetylene according to the sachsse-bartholome method | |
EP2406000A1 (en) | Method and apparatus for a constant steam generation from the waste heat of an alkane dehydrogenation | |
DE19620378C2 (en) | pyrolysis | |
US7741501B2 (en) | Process for heterogeneously catalyzed hydrogenation | |
DE102010042678B4 (en) | Apparatus and method for generating mechanical and electrical energy from a fuel | |
WO2018041728A1 (en) | Method and device for removing organic sulphur compounds from hydrogen-rich gases | |
EP2217685A1 (en) | Method for desulfurizing ingredient materials containing olefin |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 07727975 Country of ref document: EP Kind code of ref document: A1 |
|
WWE | Wipo information: entry into national phase |
Ref document number: 200780013847.1 Country of ref document: CN |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
WWE | Wipo information: entry into national phase |
Ref document number: 1020087026385 Country of ref document: KR |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2007727975 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2008145106 Country of ref document: RU |