JP4409937B2 - 糖類の接触水素化のための、SiO2をベースとする担体材料上のルテニウム触媒 - Google Patents
糖類の接触水素化のための、SiO2をベースとする担体材料上のルテニウム触媒 Download PDFInfo
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- JP4409937B2 JP4409937B2 JP2003503349A JP2003503349A JP4409937B2 JP 4409937 B2 JP4409937 B2 JP 4409937B2 JP 2003503349 A JP2003503349 A JP 2003503349A JP 2003503349 A JP2003503349 A JP 2003503349A JP 4409937 B2 JP4409937 B2 JP 4409937B2
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- Prior art keywords
- ruthenium
- catalyst
- support material
- weight
- hydrogenation
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- 239000003054 catalyst Substances 0.000 title claims abstract description 115
- 229910052707 ruthenium Inorganic materials 0.000 title claims abstract description 70
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 title claims abstract description 69
- 239000000463 material Substances 0.000 title claims abstract description 58
- 238000009903 catalytic hydrogenation reaction Methods 0.000 title claims abstract description 9
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 title claims description 26
- 239000000377 silicon dioxide Substances 0.000 title claims description 10
- 235000012239 silicon dioxide Nutrition 0.000 title claims description 7
- 235000000346 sugar Nutrition 0.000 title description 3
- 229910052681 coesite Inorganic materials 0.000 title 1
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- 229910052682 stishovite Inorganic materials 0.000 title 1
- 150000008163 sugars Chemical class 0.000 title 1
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- 238000000034 method Methods 0.000 claims abstract description 45
- 150000002772 monosaccharides Chemical class 0.000 claims abstract description 22
- 239000007787 solid Substances 0.000 claims abstract description 22
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 21
- 238000001035 drying Methods 0.000 claims abstract description 21
- 239000001257 hydrogen Substances 0.000 claims abstract description 21
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 21
- 238000004519 manufacturing process Methods 0.000 claims abstract description 21
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- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 claims description 3
- OJLCQGGSMYKWEK-UHFFFAOYSA-K ruthenium(3+);triacetate Chemical compound [Ru+3].CC([O-])=O.CC([O-])=O.CC([O-])=O OJLCQGGSMYKWEK-UHFFFAOYSA-K 0.000 claims description 2
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- 229910052500 inorganic mineral Inorganic materials 0.000 description 3
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- VQHSOMBJVWLPSR-JVCRWLNRSA-N lactitol Chemical compound OC[C@H](O)[C@@H](O)[C@@H]([C@H](O)CO)O[C@@H]1O[C@H](CO)[C@H](O)[C@H](O)[C@H]1O VQHSOMBJVWLPSR-JVCRWLNRSA-N 0.000 description 1
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- 230000001590 oxidative effect Effects 0.000 description 1
- 238000010979 pH adjustment Methods 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 150000002972 pentoses Chemical class 0.000 description 1
- 238000002459 porosimetry Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 230000007420 reactivation Effects 0.000 description 1
- RADGOBKLTHEUQO-UHFFFAOYSA-N ruthenium(4+) Chemical compound [Ru+4] RADGOBKLTHEUQO-UHFFFAOYSA-N 0.000 description 1
- 239000000523 sample Substances 0.000 description 1
- 238000010517 secondary reaction Methods 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
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- 150000003538 tetroses Chemical class 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
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- 239000002912 waste gas Substances 0.000 description 1
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Description
i)非晶質二酸化ケイ素をベースとする担体材料を、低分子量ルテニウム化合物のハロゲンを含まない水溶液で1回以上処理し、次にその処理した担体材料を200℃以下、好ましくは≦180℃、特には≦150℃で乾燥し、
ii)i)で得られた固体を100〜350℃、好ましくは150〜350℃、特には200〜320℃で水素によって還元し、
工程ii)を工程i)の直後に実施することにより得られるルテニウム触媒によって、上記目的が達成されることを見出した。
1.方法A:非焼成粉末状ハロゲン非含有触媒
所定量の個々の担体材料に、個々の担体材料が取り込むことができる最大量の硝酸ニトロシルルテニウム(III)水溶液を含浸させた。個々の担体材料が取り込むことができる最大量は、基準サンプルで予め求めた。担体材料内で所望のルテニウム濃度が得られるように、各場合で溶液濃度を計算した。
乾燥を回転式球形乾燥機で行った以外は、方法Aの手順と同様の操作を行った。残留含水量は1重量%以下であった。
乾燥後に得られた固体を空気流下で400℃にて4時間加熱してから、水素化を行った以外は、方法Bの手順と同様の操作を行った。
硝酸ニトロシルルテニウム(III)に代えて塩化ルテニウム(III)を用いて、方法Bの手順と同様の操作を行った。
所定量の円柱形担体材料押出物(直径:4mm、長さ:3〜10mm)に、個々の担体材料が取り込むことができる最大量の硝酸ニトロシルルテニウム(III)水溶液を含浸させた。個々の担体材料が取り込むことができる最大量は、基準サンプルで予め求めた。担体材料内で所望のルテニウム濃度が得られるように、各場合で溶液濃度を計算した。
1)下記の特性を有するシリカゲル粉末
SiO2含有量:>99.95重量%、
比BET表面積:523m2/g、
取り込み水分量:1.4mL/g、
孔げき量:0.75mL/g(DIN66134による窒素ポロシメトリーによって測定)、
所定孔径:60Å、
粒径:63〜200μm;
2)下記の特性を有するα−酸化アルミニウム粉末
Al2O3含有量:>99.95重量%、
比BET表面積:7m2/g、
取り込み水分量:0.84mL/g、
粒径<100μm;
3)下記の特性を有するθ−酸化アルミニウム粉末
Al2O3含有量:>99.95重量%、
比BET表面積:80m2/g、
取り込み水分量:1.05mL/g、
孔げき量:0.67mL/g(DIN66134)、
粒径:<100μm;
4)下記の特性を有する酸化チタン
TiO2含有量:>99.9重量%、
比BET表面積:325m2/g、
取り込み水分量:0.84mL/g、
粒径:<63μm;
5)下記の特性を有するシリカゲルを含有するシリカゲル押出物(d=4mm、L=1〜10mm)
SiO2含有量:>99.5重量%(0.3重量%のNa2O)、
比BET表面積:169m2/g、
取り込み水分量:0.95mL/g、
孔げき量:0.7mL/g(DIN66134)。
一般的水素化法
濃度30重量%のキシロース水溶液1200mLと個々の触媒3gとを、撹拌機、サンプリング器具および水素圧力調整器を取り付けた2.5リットルのオートクレーブに入れた。オートクレーブに窒素を充填した。次にそれを100バールの水素で加圧し、加熱して90℃とした。反応中、反応混合物を1000rpmで撹拌した。反応中の転化率を測定するため、定期的にサンプル採取を行い、HPLCによる分析を行って、キシロース、キシリトールおよび他の生成物の含有量を測定した。10時間以内に反応を停止した。表2には、最大収率に達するのに必要な時間を示している。その表には、約0.5%(絶対値)の精度まで求めることができたキシリトール形成に関する選択性も示している。
IIで示した一般的水素化法と類似の手順を用いて、個々の触媒3g存在下に、50バールの水素下で120℃にて、濃度30%の個々の単糖類または二糖類の水溶液1200mLを水素化した。転化率および選択性を、IIで記載のようにHPLCによって測定した。表3に、最大転化率(>99.8%)に達するのに必要な時間を示している。さらに、所望の糖アルコールの形成に関する選択性も示している。
リアクターは、触媒C8を入れた加熱可能なステンレス製反応管を使用した。その反応装置には、原料用の供給ポンプ、循環ポンプ、サンプリング器具および液位調整器および廃ガス調整器を有する分離装置も取り付けた。
Claims (15)
- i)非晶質二酸化ケイ素をベースとする担体材料を、低分子量ルテニウム化合物のハロゲンを含まない水溶液で1回以上処理し、次にその処理した担体材料を200℃以下で乾燥し、
ii)i)で得られた前記固体を100〜350℃で水素によって還元し、
工程ii)を工程i)の直後に実施することにより得られ、触媒中のルテニウム含有量が担体材料基準で0.1〜5重量%である、単糖類および二糖類を接触水素化することで糖アルコールを製造するためのルテニウム触媒。 - 前記非晶質二酸化ケイ素をベースとする担体が50〜700m2/gの範囲のBET表面積を有する請求項1に記載のルテニウム触媒。
- 前記二酸化ケイ素をベースとする担体材料が少なくとも90重量%の二酸化ケイ素およびAl2O3換算で1重量%未満の酸化アルミニウムを含む請求項1または2に記載のルテニウム触媒。
- 工程i)で使用される前記ルテニウム化合物が硝酸ニトロシルルテニウム(III)、酢酸ルテニウム(III)、ルテニウム(IV)酸ナトリウムおよびルテニウム(IV)酸カリウムから選択される請求項1〜3のいずれか1項に記載のルテニウム触媒。
- i)から得られ、還元ii)に使用される前記固体が、固体総重量基準で5重量%未満の含水量を有する請求項1〜4のいずれか1項に記載のルテニウム触媒。
- 工程i)における乾燥を、前記処理済み担体材料を運動させながら実施する請求項1〜5のいずれか1項に記載のルテニウム触媒。
- 触媒総重量基準で0.05重量%未満のハロゲンを含み、
非晶質二酸化ケイ素をベースとする担体材料ならびに
担体材料の重量基準で0.1〜5重量%の量の、原子レベルで分散した形態および/または担体上のルテニウム粒子の形態で存在するルテニウム元素
を含有するルテニウム触媒であって、
該触媒が10nmを超える直径を有するルテニウムの粒子および/または凝集塊を実質的に含まない、請求項1〜6のいずれか1項に記載のルテニウム触媒。 - 請求項1〜7のいずれか1項に記載のルテニウム触媒の製造方法であって、
i)非晶質二酸化ケイ素をベースとする担体材料を低分子量ルテニウム化合物のハロゲンを含まない水溶液で1回以上処理し、次にその処理した担体材料を200℃以下で乾燥する工程、
ii)i)で得られた前記固体を100〜350℃で水素によって還元する工程
を有し、工程ii)を工程i)の直後に実施する方法。 - ソルビトールの製造を除く、対応する単糖類および二糖類の接触水素化による糖アルコールの製造における、請求項1〜7のいずれか1項に記載の触媒の使用。
- ソルビトールの製造方法を除く、不均一系ルテニウム触媒上にて液相中の対応する単糖類およびオリゴ糖類の接触水素化によって糖アルコールを製造する方法であって、前記不均一系ルテニウム触媒が請求項1〜7のいずれか1項に記載のルテニウム触媒から選択される、前記方法。
- 前記単糖類またはオリゴ糖類を、pHが4〜10の範囲である水溶液として用いる請求項10に記載の方法。
- 前記水素化を10〜500バールの範囲の水素分圧で実施する請求項10または11に記載の方法。
- 前記水素化を40〜250℃で行う請求項10〜12のいずれか1項に記載の方法。
- 前記水素化を固定触媒床上で行う請求項10〜13のいずれか1項に記載の方法。
- 前記水素化を、前記触媒が懸濁液の形態で存在する液相中で行う請求項10〜13のいずれか1項に記載の方法。
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DE2001128205 DE10128205A1 (de) | 2001-06-11 | 2001-06-11 | Ruthenium-Katalysatoren |
PCT/EP2002/006346 WO2002100537A2 (de) | 2001-06-11 | 2002-06-10 | Ruthenium-katalysatoren auf einem träger auf si02-basis für die katalytische hydrierung von sacchariden |
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WO2005021475A1 (en) * | 2003-09-03 | 2005-03-10 | Sk Corporation | Method for preparing sugar alcohols by catalytic hydrogenation of sugars |
JP4813830B2 (ja) * | 2004-10-14 | 2011-11-09 | 三菱重工業株式会社 | 排ガス処理触媒、排ガス処理方法および排ガス処理装置 |
DE102005029200A1 (de) | 2005-06-22 | 2006-12-28 | Basf Ag | Katalysator und Verfahren zur Hydrierung von hydrierbare Gruppen enthaltenden organischen Verbindungen |
DE102005030728A1 (de) * | 2005-07-01 | 2007-01-04 | Lanxess Deutschland Gmbh | Verfahren zur Ruthenium-katalysierten Oxidation von Alkoholen mit Hypochlorit |
DE102005040286A1 (de) * | 2005-08-25 | 2007-03-01 | Basf Ag | Mechanisch stabiler Katalysator auf Basis von alpha-Aluminiumoxid |
EP1921057B1 (en) * | 2005-08-26 | 2012-01-25 | Asahi Kasei Chemicals Corporation | Process for production of cycloolefin |
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2001
- 2001-06-11 DE DE2001128205 patent/DE10128205A1/de not_active Withdrawn
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- 2002-06-10 AU AU2002319210A patent/AU2002319210A1/en not_active Abandoned
- 2002-06-10 US US10/480,284 patent/US7618917B2/en not_active Expired - Fee Related
- 2002-06-10 RU RU2004100530A patent/RU2322293C2/ru not_active IP Right Cessation
- 2002-06-10 EP EP02748756A patent/EP1399255B1/de not_active Expired - Lifetime
- 2002-06-10 EP EP20080166458 patent/EP2030680B1/de not_active Revoked
- 2002-06-10 DK DK02748756T patent/DK1399255T3/da active
- 2002-06-10 WO PCT/EP2002/006346 patent/WO2002100537A2/de active Application Filing
- 2002-06-10 CN CNB028136691A patent/CN100435942C/zh not_active Expired - Fee Related
- 2002-06-10 JP JP2003503349A patent/JP4409937B2/ja not_active Expired - Fee Related
- 2002-06-10 BR BR0210333A patent/BR0210333A/pt not_active IP Right Cessation
- 2002-06-10 AT AT02748756T patent/ATE411104T1/de not_active IP Right Cessation
- 2002-06-10 KR KR1020037016160A patent/KR100893794B1/ko not_active IP Right Cessation
- 2002-06-10 MX MXPA03011157A patent/MXPA03011157A/es not_active Application Discontinuation
- 2002-06-10 DE DE50212904T patent/DE50212904D1/de not_active Expired - Lifetime
- 2002-06-10 ES ES02748756T patent/ES2312596T3/es not_active Expired - Lifetime
- 2002-06-10 PT PT02748756T patent/PT1399255E/pt unknown
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DE50212904D1 (de) | 2008-11-27 |
US7618917B2 (en) | 2009-11-17 |
DK1399255T3 (da) | 2009-02-02 |
KR100893794B1 (ko) | 2009-04-20 |
KR20040007679A (ko) | 2004-01-24 |
AU2002319210A1 (en) | 2002-12-23 |
BR0210333A (pt) | 2006-04-04 |
CN100435942C (zh) | 2008-11-26 |
EP1399255A2 (de) | 2004-03-24 |
PT1399255E (pt) | 2008-11-27 |
WO2002100537A3 (de) | 2003-07-10 |
DE10128205A1 (de) | 2002-12-12 |
US20080210222A1 (en) | 2008-09-04 |
MXPA03011157A (es) | 2004-02-26 |
RU2004100530A (ru) | 2005-06-20 |
JP2004534638A (ja) | 2004-11-18 |
WO2002100537A2 (de) | 2002-12-19 |
EP1399255B1 (de) | 2008-10-15 |
CN1524016A (zh) | 2004-08-25 |
ES2312596T3 (es) | 2009-03-01 |
EP2030680A1 (de) | 2009-03-04 |
EP2030680B1 (de) | 2014-07-02 |
US20040176619A1 (en) | 2004-09-09 |
RU2322293C2 (ru) | 2008-04-20 |
ATE411104T1 (de) | 2008-10-15 |
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