RU2006143086A - METHOD FOR STRUCTURED FILLING OF CONTACT PIPES BEAM OF CONTACT PIPES - Google Patents
METHOD FOR STRUCTURED FILLING OF CONTACT PIPES BEAM OF CONTACT PIPES Download PDFInfo
- Publication number
- RU2006143086A RU2006143086A RU2006143086/15A RU2006143086A RU2006143086A RU 2006143086 A RU2006143086 A RU 2006143086A RU 2006143086/15 A RU2006143086/15 A RU 2006143086/15A RU 2006143086 A RU2006143086 A RU 2006143086A RU 2006143086 A RU2006143086 A RU 2006143086A
- Authority
- RU
- Russia
- Prior art keywords
- catalyst
- package
- contact
- filling
- filled
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract 20
- IHPYMWDTONKSCO-UHFFFAOYSA-N 2,2'-piperazine-1,4-diylbisethanesulfonic acid Chemical compound OS(=O)(=O)CCN1CCN(CCS(O)(=O)=O)CC1 IHPYMWDTONKSCO-UHFFFAOYSA-N 0.000 title 1
- 239000007990 PIPES buffer Substances 0.000 title 1
- 239000003054 catalyst Substances 0.000 claims abstract 20
- 239000000203 mixture Substances 0.000 claims abstract 7
- 238000004806 packaging method and process Methods 0.000 claims abstract 5
- 239000003795 chemical substances by application Substances 0.000 claims 1
Classifications
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- 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
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- 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
- B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
- B01J8/003—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor in a downward flow
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- 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
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
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- 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
-
- 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
- B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
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- 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
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- 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
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
- B01J2208/00212—Plates; Jackets; Cylinders
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- 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
- B01J2208/00743—Feeding or discharging of solids
- B01J2208/00752—Feeding
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- 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
- B01J2208/00743—Feeding or discharging of solids
- B01J2208/00769—Details of feeding or discharging
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- 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
- B01J2208/00796—Details of the reactor or of the particulate material
- B01J2208/00805—Details of the particulate material
- B01J2208/00814—Details of the particulate material the particulate material being provides in prefilled containers
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- 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
- B01J2208/02—Processes carried out in the presence of solid particles; Reactors therefor with stationary particles
- B01J2208/023—Details
- B01J2208/024—Particulate material
- B01J2208/025—Two or more types of catalyst
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- 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
- B01J2219/30—Details relating to random packing elements
- B01J2219/308—Details relating to random packing elements filling or discharging the elements into or from packed columns
- B01J2219/3086—Filling of the packing elements into the column or vessel, e.g. using a tube
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- 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
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
- B01J23/888—Tungsten
- B01J23/8885—Tungsten containing also molybdenum
-
- 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
- B01J2523/00—Constitutive chemical elements of heterogeneous catalysts
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- B01J35/19—
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- B01J35/50—
Abstract
1. Способ структурированного заполнения контактных труб пучка контактных труб, при котором отдельные контактные трубы пучка контактных труб заполняют единым образом снизу вверх по отрезкам различимыми друг от друга составами катализаторных формованных изделий, отличающийся тем, что для получения определенного отрезка заполнения в контактных трубах сначала создают единые количественные порции соответствующего состава из катализаторных формованных изделий, обертыванием таких порций упаковочным средством получают заполненные единым количеством состава катализаторных формованных изделий упаковки и опорожняют в каждую из индивидуальных контактных труб одно число упаковок.2. Способ по п.1, отличающийся тем, что количество состава катализаторных формованных изделий в одной упаковке составляет 50 г до 5 кг.3. Способ по п.1, отличающийся тем, что продольное распространение подлежащих заполнению катализаторных формованных изделий составляет от 1 мм до 20 мм.4. Способ по п.1, отличающийся тем, что заполненные контактные трубы имеют, по меньшей мере, три различимых друг от друга отрезков заполнения.5. Способ по одному из пп.1-4, отличающийся тем, что соотношение внутреннего диаметра D контактной трубы к продольному распространению L, содержащихся в одной упаковке катализаторных формованных изделий, составляет от 2:1 до 20:1.6. Способ по п.1, отличающийся тем, что активная масса содержащихся в одной упаковке катализаторных формованных изделий представляет собой содержащий Мо, Bi и Fe и/или Мо и V оксид мультиметаллов.7. Способ по п.1, отличающийся тем, что количественная порция упаковки такова, что ее опорожнением в контактную тр�1. A method of structured filling of the contact tubes of a bundle of contact tubes, in which the individual contact tubes of the bundle of contact tubes are filled in a uniform manner from bottom to top along the segments with distinguishable compositions of catalyst molded articles, characterized in that to obtain a certain segment of filling in the contact tubes, uniform quantitative portions of the corresponding composition of the catalyst shaped articles, by wrapping such portions with a packaging means, packages filled with a single amount of the composition of the catalyst shaped articles are obtained and one number of packages are emptied into each of the individual contact tubes. 2. The method according to claim 1, characterized in that the amount of the composition of the catalyst shaped bodies in one package is 50 g to 5 kg. The method according to claim 1, characterized in that the longitudinal spread of the catalyst shaped bodies to be filled is from 1 mm to 20 mm. The method according to claim 1, characterized in that the filled contact tubes have at least three distinct filling segments. A method according to one of claims 1 to 4, characterized in that the ratio of the inner diameter D of the contact tube to the longitudinal expansion L of the catalyst shaped bodies contained in one package is from 2: 1 to 20: 1.6. The method according to claim 1, characterized in that the active mass of the catalyst shaped bodies contained in one package is a multimetal oxide containing Mo, Bi and Fe and / or Mo and V. The method according to claim 1, characterized in that the quantitative portion of the package is such that emptying it into a contact tube
Claims (15)
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US56869904P | 2004-05-07 | 2004-05-07 | |
DE102004023249.0 | 2004-05-07 | ||
DE102004023249A DE102004023249A1 (en) | 2004-05-07 | 2004-05-07 | Process to insert selected catalyst rings into battery of reactor tubes followed by manual removal as required |
US60/568,699 | 2004-05-07 |
Publications (2)
Publication Number | Publication Date |
---|---|
RU2006143086A true RU2006143086A (en) | 2008-06-20 |
RU2393915C2 RU2393915C2 (en) | 2010-07-10 |
Family
ID=34178117
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
RU2006143086/15A RU2393915C2 (en) | 2004-05-07 | 2005-04-22 | Method of structured filling of contact tubes of contact tube bundle and package produced on wrapping by quantitative portion of formed catalyst product composition |
Country Status (6)
Country | Link |
---|---|
JP (1) | JP4768726B2 (en) |
KR (1) | KR101431365B1 (en) |
CN (3) | CN103894117A (en) |
DE (1) | DE102004023249A1 (en) |
RU (1) | RU2393915C2 (en) |
ZA (1) | ZA200610181B (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102007017080A1 (en) * | 2007-04-10 | 2008-10-16 | Basf Se | Method for feeding a longitudinal section of a contact tube |
DE102007028332A1 (en) | 2007-06-15 | 2008-12-18 | Basf Se | A method for feeding a reactor with a fixed catalyst bed comprising at least annular shaped catalyst bodies K. |
DE102007028333A1 (en) | 2007-06-15 | 2008-12-18 | Basf Se | Method for introducing a subset taken from at least one production batch of annular shell catalysts K into a reaction tube of a tube bundle reactor |
DE202008004922U1 (en) | 2008-04-10 | 2009-08-20 | Süd-Chemie AG | Feeding system for tube bundle reactors |
DE102014016203A1 (en) | 2014-11-03 | 2016-05-19 | Clariant International Ltd. | Feeding system for feeding a tube bundle reactor |
EP3112014A1 (en) * | 2015-06-30 | 2017-01-04 | Shell Internationale Research Maatschappij B.V. | Method of loading a particulate material into a reactor |
WO2021048373A1 (en) * | 2019-09-13 | 2021-03-18 | Hte Gmbh The High Throughput Experimentation Company | Method for filling reactors and for examining catalytic reactors |
Family Cites Families (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL62754C (en) * | 1941-01-27 | |||
IT955185B (en) * | 1972-04-29 | 1973-09-29 | Saes Getter Spa | CATALYTIC CARTRIDGE |
KR830000312B1 (en) * | 1978-03-13 | 1983-03-02 | 유씨비, 에스. 에이. | Plastic container body for pressurized carbonated beverage |
US4402643A (en) * | 1981-02-18 | 1983-09-06 | Ppg Industries, Inc. | Catalyst loader |
JPS63197533A (en) * | 1987-12-28 | 1988-08-16 | ケミカル・リサーチ・アンド・ライセンシング・カンパニー | Catalytic distillation catalyst |
WO1990002603A1 (en) * | 1988-09-02 | 1990-03-22 | Gebrüder Sulzer Aktiengesellschaft | Device for carrying out catalytic reactions |
US5266546A (en) * | 1992-06-22 | 1993-11-30 | Chemical Research & Licensing Company | Catalytic distillation machine |
EP0631813B1 (en) * | 1993-06-30 | 1998-01-07 | Sulzer Chemtech AG | Catalysing fixed-bed reactor |
DE4442346A1 (en) * | 1994-11-29 | 1996-05-30 | Basf Ag | Process for producing a catalyst consisting of a support body and a catalytically active oxide mass applied to the surface of the support body |
WO1998014392A1 (en) * | 1996-10-22 | 1998-04-09 | Comardo Mathis P | Catalytic reactor charging system and method |
JP3891726B2 (en) * | 1999-04-12 | 2007-03-14 | 三井化学株式会社 | Filling method of organopolymer siloxane catalyst |
DE19934324A1 (en) * | 1999-07-21 | 2000-09-07 | Basf Ag | Apparatus for filling tubular reactors with catalyst particles comprises a filling tube that can be moved in a frame structure in two directions |
AU2001265326A1 (en) * | 2000-06-07 | 2001-12-17 | Abb Lummus Global Inc. | Heat exchanger/reactor apparatus |
CN1172823C (en) * | 2001-05-30 | 2004-10-27 | 中国石油化工股份有限公司 | Packing bag and its application in packing catalyst |
JP4092090B2 (en) * | 2001-06-26 | 2008-05-28 | 株式会社日本触媒 | Solid particle packed reactor and catalytic gas phase oxidation method using the reactor |
US7182778B2 (en) * | 2001-11-01 | 2007-02-27 | Gel Tech Solutions, Inc. | Conforming thermal pack |
-
2004
- 2004-05-07 DE DE102004023249A patent/DE102004023249A1/en not_active Withdrawn
-
2005
- 2005-04-22 CN CN201410148505.2A patent/CN103894117A/en active Pending
- 2005-04-22 CN CNA2005800146017A patent/CN1956773A/en active Pending
- 2005-04-22 JP JP2007511930A patent/JP4768726B2/en active Active
- 2005-04-22 RU RU2006143086/15A patent/RU2393915C2/en active
- 2005-04-22 KR KR1020127028080A patent/KR101431365B1/en active IP Right Grant
- 2005-04-22 CN CN201410148068.4A patent/CN103908927A/en active Pending
-
2006
- 2006-12-05 ZA ZA200610181A patent/ZA200610181B/en unknown
Also Published As
Publication number | Publication date |
---|---|
JP2007536078A (en) | 2007-12-13 |
KR101431365B1 (en) | 2014-08-18 |
CN1956773A (en) | 2007-05-02 |
ZA200610181B (en) | 2008-05-28 |
CN103894117A (en) | 2014-07-02 |
CN103908927A (en) | 2014-07-09 |
RU2393915C2 (en) | 2010-07-10 |
DE102004023249A1 (en) | 2005-03-10 |
JP4768726B2 (en) | 2011-09-07 |
KR20120134146A (en) | 2012-12-11 |
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