KR840000273A - 안티모네이트 촉매의 제조방법 - Google Patents
안티모네이트 촉매의 제조방법 Download PDFInfo
- Publication number
- KR840000273A KR840000273A KR1019820003028A KR820003028A KR840000273A KR 840000273 A KR840000273 A KR 840000273A KR 1019820003028 A KR1019820003028 A KR 1019820003028A KR 820003028 A KR820003028 A KR 820003028A KR 840000273 A KR840000273 A KR 840000273A
- Authority
- KR
- South Korea
- Prior art keywords
- catalyst
- support material
- slurry
- mixed
- compound
- Prior art date
Links
- 239000003054 catalyst Substances 0.000 title claims 17
- 238000004519 manufacturing process Methods 0.000 title 1
- 238000000034 method Methods 0.000 claims 10
- 150000001875 compounds Chemical class 0.000 claims 8
- 239000012041 precatalyst Substances 0.000 claims 8
- 239000000463 material Substances 0.000 claims 7
- 239000002002 slurry Substances 0.000 claims 6
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims 3
- 229910052783 alkali metal Inorganic materials 0.000 claims 2
- 150000001340 alkali metals Chemical class 0.000 claims 2
- 229910052796 boron Inorganic materials 0.000 claims 2
- 239000007788 liquid Substances 0.000 claims 2
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 claims 2
- 229910052776 Thorium Inorganic materials 0.000 claims 1
- 229910052785 arsenic Inorganic materials 0.000 claims 1
- 229910052804 chromium Inorganic materials 0.000 claims 1
- 229910021485 fumed silica Inorganic materials 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 claims 1
- 229910052749 magnesium Inorganic materials 0.000 claims 1
- 229910052748 manganese Inorganic materials 0.000 claims 1
- 229910052750 molybdenum Inorganic materials 0.000 claims 1
- 230000003647 oxidation Effects 0.000 claims 1
- 238000007254 oxidation reaction Methods 0.000 claims 1
- 230000001590 oxidative effect Effects 0.000 claims 1
- 229910052761 rare earth metal Inorganic materials 0.000 claims 1
- 150000002910 rare earth metals Chemical class 0.000 claims 1
- 239000000377 silicon dioxide Substances 0.000 claims 1
- 238000007613 slurry method Methods 0.000 claims 1
- 239000012265 solid product Substances 0.000 claims 1
- 229910052718 tin Inorganic materials 0.000 claims 1
- 229910052721 tungsten Inorganic materials 0.000 claims 1
- 229910052720 vanadium Inorganic materials 0.000 claims 1
- 229910052726 zirconium Inorganic materials 0.000 claims 1
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
- 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
-
- 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
- B01J23/843—Arsenic, antimony or bismuth
- B01J23/8435—Antimony
-
- 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
- B01J23/18—Arsenic, antimony or bismuth
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0236—Drying, e.g. preparing a suspension, adding a soluble salt and drying
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
내용 없음
Description
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
Claims (12)
- 하기 (1)단계에서의 공급원 화합물과 혼합하는 지지물질이 훈연 촉매 지지물질 및 촉매 지지물 졸(sol)로 이루어짐을 특징으로 하여, (1) 안티모. 이트-기준 산화 작화합물의 모든성분을 함유한 공급원화합물 및 상기 지지물질을 혼합하여 전-촉매 슬러리를 형성시키고, (2) 상기 전-촉매 슬러리에서 액체를 제거하여 전-촉매를 형성시킨 다음, (3) 상기 전-촉매를 고온에서 가열하여 촉매를 형성시키는, 촉매지체상에 지지된 상기 산화착화합물을 함유하는 유동상촉매를 제조하는 단일슬러리 방법.
- 제1항에 있어서, 실리카 졸 및 훈연 실리카를 상기 공급원 화합물과 혼합시키는 방법.
- 제2항에 있어서, 상기 훈연 실리카 및 상기 실리카졸을 상기 공급원 화합물과 혼합하기 전에 함께 혼합하는 방법.
- 제1항에 있어서, 상기 안티모네이트-기준 촉매가 다음 일반식을 갖는 방법.AaBbSbcOx상기식에서 : A는 Fe, U, Sn, Th, Cr, Ti, Ce, Mg 및/또는 Mn이고, B는 Zr, V, W, Mo, As, B, Cu, Pr, Al, Te, 희토류금속, 알카리금속, Mg 및/또는 Bi 이외의 알카리 토금속이고, a는 0내지 10이고 b는 0내지 10이고 c는 0.1내지 40이고, A가 Sn 및/또는 Ti가 아닐경우 a+b<c이고 x는 존재하는 다른 원소에서 요구되는 원자가로써 결정된 수이다.
- 제4항에 있어서, a는 0.1 내지 10이고, b는 0.01 내지 10이고, c는 0.1 내지 20인 방법.
- 제5항에 있어서, 4b=a+c인 방법.
- 제6항에 있어서, A가 Fe 및/또는 Sn인 방법.
- 제7항에 있어서, b/c는 1/10내지 5/10인 방법.
- 제8항에 있어서, b/c는 2/10내지 4/10인 방법.
- 청구범위(1)의 방법에 의해 제조된 촉매.
- 청구범위(4)의 방법에 의해 제조된 촉매.
- 하기(1)단계에서의 공급된 화합물과 혼합하는 지지물이 훈연 촉매 지지물질 및 촉매 지지물질 졸로 이루어지고 하기 전-촉매 슬러리가 훈연 촉매 지지물질 및 하나이상의 공급원 화합물을 함유한 슬러리-유도 고체생성물질을 첨가함이 없이 형성시킴을 특징으로 하여, (1) 안티모네이트-기준 산화착화합물의 모든 성분을 함유한 공급원 화합물 및 상기 지지물질을 혼합하여 전-촉매 슬러리를 형성시키고, (2) 상기 전-촉매 슬러리에서 액체를 제거하여 전-촉매를 형성시킨다음(3) 상기 전-촉매를 고온에서 가열하여 촉매를 형성시키는, 촉매지지체상에 지지된 상기 산화착화합물을 함유하는 유동상촉매를 제조하는 방법.※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US281160 | 1981-07-08 | ||
US281,160 | 1981-07-08 | ||
US06/281,160 US4377500A (en) | 1981-07-08 | 1981-07-08 | Catalysts |
Publications (2)
Publication Number | Publication Date |
---|---|
KR840000273A true KR840000273A (ko) | 1984-02-18 |
KR880001496B1 KR880001496B1 (ko) | 1988-08-16 |
Family
ID=23076186
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR8203028A KR880001496B1 (ko) | 1981-07-08 | 1982-07-07 | 안티모네이트-기본 촉매의 제조방법 |
Country Status (12)
Country | Link |
---|---|
US (1) | US4377500A (ko) |
EP (1) | EP0069439B1 (ko) |
JP (1) | JPS5811045A (ko) |
KR (1) | KR880001496B1 (ko) |
BR (1) | BR8203314A (ko) |
CA (1) | CA1177468A (ko) |
DE (1) | DE3267980D1 (ko) |
ES (1) | ES8303115A1 (ko) |
IN (1) | IN158093B (ko) |
MX (1) | MX159067A (ko) |
PT (1) | PT75207B (ko) |
TR (1) | TR21656A (ko) |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0115646A1 (en) * | 1983-02-08 | 1984-08-15 | Stamicarbon B.V. | Oxidation catalysts and their preparation procedure |
JPS60166037A (ja) * | 1984-02-07 | 1985-08-29 | Nitto Chem Ind Co Ltd | シリカ担持アンチモン含有酸化物触媒の製法 |
JPS61231291A (ja) * | 1985-04-01 | 1986-10-15 | 日本鋼管株式会社 | スパイラル状リブ付被覆ケ−ブル |
JPH022734Y2 (ko) * | 1985-05-08 | 1990-01-23 | ||
JPH0763628B2 (ja) * | 1987-02-24 | 1995-07-12 | 日東化学工業株式会社 | アンチモン・テルル含有金属酸化物触媒の製法 |
US6395676B2 (en) | 1994-02-22 | 2002-05-28 | The Standard Oil Company | Process for the preparation of fluid bed vinyl acetate catalyst |
ES2321162T3 (es) | 1997-04-15 | 2009-06-03 | Csir | Compuestos y composiciones farmaceuticas que tienen actividad supresora del apetito. |
GB2396815B (en) | 1999-10-27 | 2004-09-08 | Phytopharm Plc | A composition comprising a pregnenone derivative and an NSAID |
GB2363985B (en) | 2000-06-30 | 2004-09-29 | Phytopharm Plc | Extracts,compounds & pharmaceutical compositions having anti-diabetic activity and their use |
US6916763B2 (en) * | 2002-11-27 | 2005-07-12 | Solutia Inc. | Process for preparing a catalyst for the oxidation and ammoxidation of olefins |
EP1691921A1 (en) * | 2003-12-18 | 2006-08-23 | Avantium International B.V. | Catalysts for alkane or alkene oxidation and ammoxidation |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3524823A (en) * | 1965-08-30 | 1970-08-18 | Goodrich Co B F | Catalyst and method of preparing unsaturated acids and aldehydes |
US3338952A (en) * | 1965-11-15 | 1967-08-29 | Standard Oil Co | Process for the catalytic ammoxidation of olefins to nitriles |
US3431292A (en) * | 1966-12-23 | 1969-03-04 | Standard Oil Co | Olefinic nitriles by ammoxidation of olefins with promoted antimony oxideuranium oxide catalyst |
DE2050155C3 (de) * | 1970-10-13 | 1978-08-31 | Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler, 6000 Frankfurt | Verfahren zur Herstellung eines Antimon, Molybdän, Vanadin und Wolfram enthaltenden Oxydationskatalysators |
US4083804A (en) * | 1974-02-09 | 1978-04-11 | Nitto Chemical Industry Co., Ltd. | Catalyst for use in and process for preparing acrylonitrile |
GB1553801A (en) * | 1977-05-13 | 1979-10-10 | Nitto Chemical Industry Co Ltd | Process for production of attrition resistant antimony oxide containing fluidized bed catalyst having controlled particle size distribution |
US4242236A (en) * | 1979-03-29 | 1980-12-30 | Chevron Research Company | 65-130 Angstrom mean radius silica-alumina catalyst support |
US4280929A (en) * | 1979-09-17 | 1981-07-28 | Standard Oil Company | Attrition resistant-higher active component fluid bed catalysts |
-
1981
- 1981-07-08 US US06/281,160 patent/US4377500A/en not_active Expired - Fee Related
-
1982
- 1982-02-09 IN IN104/DEL/82A patent/IN158093B/en unknown
- 1982-02-10 CA CA000395968A patent/CA1177468A/en not_active Expired
- 1982-03-04 ES ES510138A patent/ES8303115A1/es not_active Expired
- 1982-03-11 JP JP57038817A patent/JPS5811045A/ja active Granted
- 1982-03-26 MX MX191992A patent/MX159067A/es unknown
- 1982-04-08 DE DE8282301865T patent/DE3267980D1/de not_active Expired
- 1982-04-08 EP EP82301865A patent/EP0069439B1/en not_active Expired
- 1982-05-03 TR TR21656A patent/TR21656A/xx unknown
- 1982-06-04 BR BR8203314A patent/BR8203314A/pt unknown
- 1982-07-07 KR KR8203028A patent/KR880001496B1/ko active
- 1982-07-07 PT PT75207A patent/PT75207B/pt unknown
Also Published As
Publication number | Publication date |
---|---|
KR880001496B1 (ko) | 1988-08-16 |
MX159067A (es) | 1989-04-14 |
IN158093B (ko) | 1986-08-30 |
TR21656A (tr) | 1985-01-18 |
PT75207B (en) | 1984-06-27 |
EP0069439A3 (en) | 1984-03-28 |
US4377500A (en) | 1983-03-22 |
EP0069439A2 (en) | 1983-01-12 |
CA1177468A (en) | 1984-11-06 |
ES510138A0 (es) | 1983-02-01 |
DE3267980D1 (en) | 1986-01-30 |
EP0069439B1 (en) | 1985-12-18 |
PT75207A (en) | 1982-08-01 |
JPS5811045A (ja) | 1983-01-21 |
JPH0316177B2 (ko) | 1991-03-04 |
BR8203314A (pt) | 1983-05-24 |
ES8303115A1 (es) | 1983-02-01 |
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