JP6279564B2 - リンドラー型触媒の部分水素化のための使用 - Google Patents
リンドラー型触媒の部分水素化のための使用 Download PDFInfo
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- JP6279564B2 JP6279564B2 JP2015517781A JP2015517781A JP6279564B2 JP 6279564 B2 JP6279564 B2 JP 6279564B2 JP 2015517781 A JP2015517781 A JP 2015517781A JP 2015517781 A JP2015517781 A JP 2015517781A JP 6279564 B2 JP6279564 B2 JP 6279564B2
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- lindlar
- cac
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- 239000003054 catalyst Substances 0.000 title claims description 54
- 238000005984 hydrogenation reaction Methods 0.000 title claims description 10
- 239000002245 particle Substances 0.000 claims description 33
- 229910052763 palladium Inorganic materials 0.000 claims description 12
- 239000000203 mixture Substances 0.000 claims description 7
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 14
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 11
- 238000000034 method Methods 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 239000011981 lindlar catalyst Substances 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- 229910000019 calcium carbonate Inorganic materials 0.000 description 5
- 239000008367 deionised water Substances 0.000 description 5
- 229910021641 deionized water Inorganic materials 0.000 description 5
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000011203 carbon fibre reinforced carbon Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 239000011541 reaction mixture Substances 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 239000002638 heterogeneous catalyst Substances 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- -1 5-hydroxy-3-methyl-penta-1,3-dienyl Chemical group 0.000 description 1
- 239000004280 Sodium formate Substances 0.000 description 1
- 238000007563 acoustic spectroscopy Methods 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 150000001345 alkine derivatives Chemical class 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007561 laser diffraction method Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000007558 optical counting method Methods 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 229940088417 precipitated calcium carbonate Drugs 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000005029 sieve analysis Methods 0.000 description 1
- HLBBKKJFGFRGMU-UHFFFAOYSA-M sodium formate Chemical compound [Na+].[O-]C=O HLBBKKJFGFRGMU-UHFFFAOYSA-M 0.000 description 1
- 235000019254 sodium formate Nutrition 0.000 description 1
- 238000004611 spectroscopical analysis Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000011550 stock solution Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
-
- 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
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/54—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/56—Platinum group metals
- B01J23/62—Platinum group metals with gallium, indium, thallium, germanium, tin or lead
- B01J23/622—Platinum group metals with gallium, indium, thallium, germanium, tin or lead with germanium, tin or lead
- B01J23/628—Platinum group metals with gallium, indium, thallium, germanium, tin or lead with germanium, tin or lead with lead
-
- 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
- B01J27/20—Carbon compounds
- B01J27/232—Carbonates
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/024—Multiple impregnation or coating
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/61—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups
- C07C45/62—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by hydrogenation of carbon-to-carbon double or triple bonds
-
- 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
- B01J37/06—Washing
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2601/00—Systems containing only non-condensed rings
- C07C2601/12—Systems containing only non-condensed rings with a six-membered ring
- C07C2601/16—Systems containing only non-condensed rings with a six-membered ring the ring being unsaturated
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Description
d50は質量メジアン径(MMD)である。全粒子の50%は、10μm以上の径である。MMDは質量基準の平均粒径と見なされる。
粒子は、通常、120μm以下である。
(i)触媒の全重量に対して85重量%(wt%)〜99.85wt%のCaCO 3、および
(ii)触媒の全重量に対して0.1wt%〜10wt%のPd、および
(iii)触媒の全重量に対して0.05wt%〜5wt%のPb
を有し、CaCO 3粒子の平均粒径(d50)が10μm〜120μmであることを特徴とする。
(i)触媒の全重量に対して89wt%〜96wt%のCaCO 3、および
(ii)触媒の全重量に対して3wt%〜7wt%のPd、および
(iii)触媒の全重量に対して1wt%〜4wt%のPb
を有し、CaCO 3粒子の平均粒径(d50)が10μm〜120μmであることを特徴とすることが好ましい。
(i)触媒の全重量に対して92.5wt%のCaCO 3、および
(ii)触媒の全重量に対して5wt%のPd、
(iii)触媒の全重量に対して2.5wt%のPb
を含み、CaCO 3粒子の平均粒径(d50)が10μm〜120μmであることを特徴とする、リンドラー型触媒(III)である。
これは、例えば沈殿法により達成される。規定の粒子径を有する炭酸カルシウムの調製については、欧州特許第1607373号明細書および同第0406662号明細書に記載されている。
[実施例1:パラジウム−鉛リンドラー触媒の調製]
40.3gの脱イオン水を40.1gの二水素テトラクロロパラデート(II)溶液(10%Pd)に加えてパラジウム原液を調製した。1N水酸化ナトリウム溶液を加えてpHを4.0に調節した。
KPL250mgを8mlのガラス製反応器に入れ、1:1のエタノール:水1.8gを加えた。実施例1の触媒(10〜100mg)および触媒毒(0.13wt%のTegochrome 22水溶液20mg)を加え、反応器を密閉した。反応器をアルゴンで5回(5barまで加圧し、その後、圧力を解放)、水素で3回(3barまで加圧し、その後、圧力を解放)パージした。反応混合物を28℃に加熱し、3barの水素に加圧し、理論消費量の100%の消費が観察されるまで600rpmで撹拌した。
Claims (3)
- リンドラー型触媒の6−ヒドロキシ−3−(5−ヒドロキシ−3−メチル−ペント−3−イン−1−イニル)−2,4,4−トリメチルシクロヘキシ−2−エノンの部分水素化のための使用であって、
前記触媒が、次の組成
(i)触媒の全重量に対して85wt%〜99.85wt%のCaCO3、
(ii)触媒の全重量に対して0.1wt%〜10wt%のPd、
(iii)触媒の全重量に対して0.05wt%〜5wt%のPb
を有し、
前記CaCO3が10μm超および120μm未満の平均粒径(d50)を有する、使用。 - 前記触媒が、次の組成
(i)触媒の全重量に対して89wt%〜96wt%のCaCO3、
(ii)触媒の全重量に対して3wt%〜7wt%のPd、
(iii)触媒の全重量に対して1wt%〜4wt%のPb
を有する、請求項1に記載の使用。 - 前記触媒が、
(i)触媒の全重量に対して92.5wt%のCaCO3、
(ii)触媒の全重量に対して5wt%のPd、
(iii)触媒の全重量に対して2.5wt%のPb
を含む、請求項1に記載の使用。
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP12173191.3 | 2012-06-22 | ||
EP12173191 | 2012-06-22 | ||
PCT/EP2013/062956 WO2013190076A1 (en) | 2012-06-22 | 2013-06-21 | New catalytic system |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2015526276A JP2015526276A (ja) | 2015-09-10 |
JP6279564B2 true JP6279564B2 (ja) | 2018-02-14 |
Family
ID=48703464
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2015517781A Active JP6279564B2 (ja) | 2012-06-22 | 2013-06-21 | リンドラー型触媒の部分水素化のための使用 |
Country Status (8)
Country | Link |
---|---|
US (1) | US9370772B2 (ja) |
EP (1) | EP2864045B1 (ja) |
JP (1) | JP6279564B2 (ja) |
KR (1) | KR102159414B1 (ja) |
CN (1) | CN104394988A (ja) |
EA (1) | EA025802B1 (ja) |
IN (1) | IN2014DN09131A (ja) |
WO (1) | WO2013190076A1 (ja) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP3275537A1 (en) | 2016-07-25 | 2018-01-31 | Omya International AG | Surface-modified calcium carbonate as carrier for transition metal-based catalysts |
US20230347325A1 (en) | 2019-09-26 | 2023-11-02 | Omya International Ag | Gncc and/or pcc as a catalytic carrier for metal species |
KR20220069988A (ko) | 2019-09-26 | 2022-05-27 | 옴야 인터내셔널 아게 | 금속 화학종을 위한 촉매 담체로서의 srcc |
EP4306210A1 (en) * | 2022-07-12 | 2024-01-17 | Omya International AG | High surface area pcc as a catalyst carrier for platinum compounds |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2780658A (en) * | 1954-01-29 | 1957-02-05 | Hoffmann La Roche | Preparation of unsaturated acyclic halides |
JPS55389A (en) * | 1978-06-02 | 1980-01-05 | Hoffmann La Roche | Cyclohexene derivative |
JPS5978126A (ja) * | 1982-10-27 | 1984-05-04 | Kuraray Co Ltd | 三重結合の部分水素添加方法 |
JP2684112B2 (ja) | 1989-06-29 | 1997-12-03 | 丸尾カルシウム株式会社 | 針状形状をしたアラゴナイト結晶形炭酸カルシウムの製造方法 |
JP3942828B2 (ja) * | 2000-07-25 | 2007-07-11 | 独立行政法人科学技術振興機構 | ボンクレキン酸前駆化合物及びその製造方法 |
CN100551826C (zh) | 2003-02-27 | 2009-10-21 | 奥多摩工业株式会社 | 球状碳酸钙及其制造方法 |
CN101628234A (zh) * | 2008-07-18 | 2010-01-20 | 赢创德固赛有限责任公司 | 催化剂的改进生产方法 |
WO2012025559A2 (en) * | 2010-08-24 | 2012-03-01 | Dsm Ip Assets B.V. | Process for the manufacture of 3,7-dimethyl-1-octen-3-ol |
US8546621B2 (en) | 2010-08-24 | 2013-10-01 | Dsm Ip Assets B.V. | Process for the manufacture of 3,7-dimethyl-1-octen-3-ol |
-
2013
- 2013-06-21 JP JP2015517781A patent/JP6279564B2/ja active Active
- 2013-06-21 EP EP13732433.1A patent/EP2864045B1/en active Active
- 2013-06-21 US US14/408,088 patent/US9370772B2/en active Active
- 2013-06-21 WO PCT/EP2013/062956 patent/WO2013190076A1/en active Application Filing
- 2013-06-21 IN IN9131DEN2014 patent/IN2014DN09131A/en unknown
- 2013-06-21 KR KR1020147035775A patent/KR102159414B1/ko active IP Right Grant
- 2013-06-21 EA EA201500030A patent/EA025802B1/ru not_active IP Right Cessation
- 2013-06-21 CN CN201380032718.2A patent/CN104394988A/zh active Pending
Also Published As
Publication number | Publication date |
---|---|
KR102159414B1 (ko) | 2020-09-24 |
CN104394988A (zh) | 2015-03-04 |
EP2864045B1 (en) | 2020-08-26 |
WO2013190076A1 (en) | 2013-12-27 |
EA201500030A1 (ru) | 2015-04-30 |
EA025802B1 (ru) | 2017-01-30 |
US20150165431A1 (en) | 2015-06-18 |
KR20150023423A (ko) | 2015-03-05 |
US9370772B2 (en) | 2016-06-21 |
EP2864045A1 (en) | 2015-04-29 |
JP2015526276A (ja) | 2015-09-10 |
IN2014DN09131A (ja) | 2015-05-22 |
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