JP2018513783A - 高耐酸性を有する水素化分解触媒 - Google Patents
高耐酸性を有する水素化分解触媒 Download PDFInfo
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- JP2018513783A JP2018513783A JP2017550192A JP2017550192A JP2018513783A JP 2018513783 A JP2018513783 A JP 2018513783A JP 2017550192 A JP2017550192 A JP 2017550192A JP 2017550192 A JP2017550192 A JP 2017550192A JP 2018513783 A JP2018513783 A JP 2018513783A
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- metal oxide
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Classifications
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- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/14—Silica and magnesia
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- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
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- B01J23/80—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 zinc, cadmium or mercury
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- 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
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- 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
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- B01J23/8892—Manganese
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- 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
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Abstract
Description
発明の概要
実施例
Claims (39)
- Cu、及びMn、Zn、Ni、またはCoのうちの少なくとも1つを含む混合金属酸化物と、
アルミナと、
シリカと、
カルシウムと、を含む、触媒。 - 触媒が、表面を含み、前記触媒の総Cu含有量に対して、前記表面でのCuのパーセントが、約0.5%〜約20%である、請求項1に記載の触媒。
- 前記触媒が、約15質量%〜約50質量%のCuを含む、請求項1または2に記載の触媒。
- 前記混合金属酸化物が、Cu及びMnを含む、請求項1〜3のいずれか1項に記載の触媒。
- 前記混合金属酸化物が、Cu及びMnを含み、前記触媒が、約2質量%〜約10質量%のMnを含む、請求項1〜4のいずれか1項に記載の触媒。
- 前記混合金属酸化物が、Cu及びZnを含む、請求項1〜5のいずれか1項に記載の触媒。
- 前記混合金属酸化物が、Cu及びZnを含み、前記触媒が、約15質量%〜約50質量%のZnを含む、請求項1〜6のいずれか1項に記載の触媒。
- 前記アルミナが、約10質量%〜約30質量%で前記触媒中に存在する、請求項1〜7のいずれか1項に記載の触媒。
- 前記シリカが、約10質量%〜約30質量%で前記触媒中に存在する、請求項1〜8のいずれか1項に記載の触媒。
- 前記シリカが、約15質量%〜約25質量%で前記触媒中に存在する、請求項1〜9のいずれか1項に記載の触媒。
- 前記カルシウムが、約2質量%〜約10質量%で前記触媒中に存在する、請求項1〜10のいずれか1項に記載の触媒。
- 前記触媒が、約0質量%〜約0.5質量%のナトリウムをさらに含む、請求項1〜11のいずれか1項に記載の触媒。
- 前記触媒が、ナトリウムを実質的に含まない、請求項1〜12のいずれか1項に記載の触媒。
- 前記触媒が、クロムを実質的に含まない、請求項1〜13のいずれか1項に記載の触媒。
- 前記触媒が、バリウムを実質的に含まない、請求項1〜14のいずれか1項に記載の触媒。
- 前記触媒が、約10m2/g〜約150m2/gのBrunauer−Emmett−Teller表面積を有する、請求項1〜15のいずれか1項に記載の触媒。
- 前記触媒が、約10m2/g〜約70m2/gのBrunauer−Emmett−Teller表面積を有する、請求項1〜16のいずれか1項に記載の触媒。
- 前記触媒が、約0.10cm3/g〜約0.80cm3/gの水銀細孔容積を有する、請求項1〜17のいずれか1項に記載の触媒。
- 前記触媒が、約0.3g/cm3〜約1.6g/cm3の充填周囲かさ密度を有する、請求項1〜18のいずれか1項に記載の触媒。
- 前記触媒が、約2.5lb/mm〜約12lb/mmの側面破壊強度を有する、請求項1〜19のいずれか1項に記載の触媒。
- 前記触媒が、円筒状、管状、多小葉、溝付き、またはうね状のうちの少なくとも1つを含む形状である、請求項1〜20のいずれか1項に記載の触媒。
- 前記触媒が粒子状触媒であり、前記粒子が約0.5mm〜約3.0mmの平均直径を有する、請求項1〜21のいずれか1項に記載の触媒。
- 前記直径が、約1.0mm〜約2.0mmである、請求項22に記載の触媒。
- 成形材料を焼成することを含み、
前記成形材料が、
Cu酸化物、及びMn、Zn、Ni、またはCoのうちの少なくとも1つの金属酸化物と、
アルミナと、
シリカゾルと、
水酸化カルシウムと、を含むペーストを成形することによって形成される、請求項1〜23のいずれか1項に記載の触媒を作製する方法。 - 前記ペーストが、溶媒をさらに含む、請求項24に記載の方法。
- 前記ペーストが、粘土材料をさらに含む、請求項24または25に記載の方法。
- 前記成形材料が、前記ペーストを錠剤化または押出加工することによって調製される、請求項24〜26のいずれか1項に記載の方法。
- 前記ペーストが、押出助剤をさらに含む、請求項24〜27のいずれか1項に記載の方法。
- 前記押出助剤が、多糖を含む、請求項24〜28のいずれか1項に記載の方法。
- 前記Cu酸化物が、酸化第二銅を含む、請求項24〜29のいずれか1項に記載の方法。
- 前記焼成が、約300℃〜約1,000℃の温度を含む、請求項24〜30のいずれか1項に記載の方法。
- 前記焼成ステップの継続時間が、約15分〜約12時間である、請求項24〜31のいずれか1項に記載の方法。
- 前記成形材料が、焼成前に乾燥される、請求項24〜31のいずれか1項に記載の方法。
- 前記成形材料が、約40℃〜約250℃の温度で乾燥される、請求項33に記載の方法。
- 供給原料及びH2を請求項1〜23のいずれか1項に記載の触媒と接触させることによる前記供給原料の水素化及び/または水素化分解を含み、
前記供給原料が、少なくとも1つのカルボニル基を含む、プロセス。 - 前記プロセスが、前記供給原料の水素化分解を含む、請求項35に記載のプロセス。
- 前記供給原料が、最も長い炭素鎖がC8〜C18の炭素数を有する化合物を含む、請求項35または36に記載のプロセス。
- 前記供給原料が、脂肪酸メチルエステルを含む、請求項35〜37のいずれか1項に記載のプロセス。
- 前記供給原料が、遊離脂肪酸を含む、請求項35〜38のいずれか1項に記載のプロセス。
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PCT/US2016/024159 WO2016154514A1 (en) | 2015-03-26 | 2016-03-25 | Hydrogenolysis catalysts with high acid tolerance |
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WO2023163899A1 (en) * | 2022-02-24 | 2023-08-31 | Basf Corporation | Nickel promoted copper alumina catalyst for slurry phase process for producing fatty alcohol |
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BR112017020321B1 (pt) | 2021-01-26 |
WO2016154514A1 (en) | 2016-09-29 |
CN107635660A (zh) | 2018-01-26 |
US10350577B2 (en) | 2019-07-16 |
US20180065108A1 (en) | 2018-03-08 |
EP3294453A1 (en) | 2018-03-21 |
EP3294453A4 (en) | 2018-10-24 |
JP6743043B2 (ja) | 2020-08-19 |
MY182072A (en) | 2021-01-18 |
US20190336944A1 (en) | 2019-11-07 |
US11077428B2 (en) | 2021-08-03 |
BR112017020321A2 (pt) | 2018-06-05 |
SA517390028B1 (ar) | 2022-05-16 |
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