JPWO2015137339A1 - 水媒体中ヒドリド異性化反応用固体触媒 - Google Patents
水媒体中ヒドリド異性化反応用固体触媒 Download PDFInfo
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- 239000011949 solid catalyst Substances 0.000 title claims abstract description 17
- 238000006317 isomerization reaction Methods 0.000 title claims abstract description 14
- 150000004678 hydrides Chemical class 0.000 title claims abstract description 13
- 239000012736 aqueous medium Substances 0.000 title description 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims abstract description 126
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims abstract description 63
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims abstract description 39
- 239000008103 glucose Substances 0.000 claims abstract description 39
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- 239000007864 aqueous solution Substances 0.000 claims abstract description 28
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- 238000010306 acid treatment Methods 0.000 claims abstract description 22
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical group O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 claims description 30
- 150000007517 lewis acids Chemical class 0.000 claims description 17
- 239000002841 Lewis acid Substances 0.000 claims description 16
- AJNVQOSZGJRYEI-UHFFFAOYSA-N digallium;oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[Ga+3].[Ga+3] AJNVQOSZGJRYEI-UHFFFAOYSA-N 0.000 claims description 8
- 229910001195 gallium oxide Inorganic materials 0.000 claims description 8
- 229910003437 indium oxide Inorganic materials 0.000 claims description 8
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- 238000004519 manufacturing process Methods 0.000 claims description 6
- WKMKTIVRRLOHAJ-UHFFFAOYSA-N oxygen(2-);thallium(1+) Chemical compound [O-2].[Tl+].[Tl+] WKMKTIVRRLOHAJ-UHFFFAOYSA-N 0.000 claims description 5
- 229910003438 thallium oxide Inorganic materials 0.000 claims description 4
- 238000006243 chemical reaction Methods 0.000 abstract description 23
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- NOEGNKMFWQHSLB-UHFFFAOYSA-N 5-hydroxymethylfurfural Chemical compound OCC1=CC=C(C=O)O1 NOEGNKMFWQHSLB-UHFFFAOYSA-N 0.000 description 10
- RJGBSYZFOCAGQY-UHFFFAOYSA-N hydroxymethylfurfural Natural products COC1=CC=C(C=O)O1 RJGBSYZFOCAGQY-UHFFFAOYSA-N 0.000 description 10
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- 229910005191 Ga 2 O 3 Inorganic materials 0.000 description 8
- 239000000243 solution Substances 0.000 description 7
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- 238000002441 X-ray diffraction Methods 0.000 description 4
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- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 238000001157 Fourier transform infrared spectrum Methods 0.000 description 3
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 3
- 229910021536 Zeolite Inorganic materials 0.000 description 3
- ILRRQNADMUWWFW-UHFFFAOYSA-K aluminium phosphate Chemical compound O1[Al]2OP1(=O)O2 ILRRQNADMUWWFW-UHFFFAOYSA-K 0.000 description 3
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 3
- 238000010304 firing Methods 0.000 description 3
- XPFVYQJUAUNWIW-UHFFFAOYSA-N furfuryl alcohol Chemical compound OCC1=CC=CO1 XPFVYQJUAUNWIW-UHFFFAOYSA-N 0.000 description 3
- 238000004128 high performance liquid chromatography Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
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- 238000005004 MAS NMR spectroscopy Methods 0.000 description 2
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- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
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- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 238000000371 solid-state nuclear magnetic resonance spectroscopy Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- DEXFNLNNUZKHNO-UHFFFAOYSA-N 6-[3-[4-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]piperidin-1-yl]-3-oxopropyl]-3H-1,3-benzoxazol-2-one Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C1CCN(CC1)C(CCC1=CC2=C(NC(O2)=O)C=C1)=O DEXFNLNNUZKHNO-UHFFFAOYSA-N 0.000 description 1
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- 229910000873 Beta-alumina solid electrolyte Inorganic materials 0.000 description 1
- 239000002028 Biomass Substances 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 238000003547 Friedel-Crafts alkylation reaction Methods 0.000 description 1
- GYHNNYVSQQEPJS-UHFFFAOYSA-N Gallium Chemical compound [Ga] GYHNNYVSQQEPJS-UHFFFAOYSA-N 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 229910010413 TiO 2 Inorganic materials 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 125000002252 acyl group Chemical group 0.000 description 1
- SMZOGRDCAXLAAR-UHFFFAOYSA-N aluminium isopropoxide Chemical compound [Al+3].CC(C)[O-].CC(C)[O-].CC(C)[O-] SMZOGRDCAXLAAR-UHFFFAOYSA-N 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000008346 aqueous phase Substances 0.000 description 1
- 229910001593 boehmite Inorganic materials 0.000 description 1
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- 230000003197 catalytic effect Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
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- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 235000003599 food sweetener Nutrition 0.000 description 1
- 229910052733 gallium Inorganic materials 0.000 description 1
- 238000007871 hydride transfer reaction Methods 0.000 description 1
- FAHBNUUHRFUEAI-UHFFFAOYSA-M hydroxidooxidoaluminium Chemical compound O[Al]=O FAHBNUUHRFUEAI-UHFFFAOYSA-M 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- -1 phosphate compound Chemical class 0.000 description 1
- 230000026731 phosphorylation Effects 0.000 description 1
- 238000006366 phosphorylation reaction Methods 0.000 description 1
- 238000006068 polycondensation reaction Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- OGHBATFHNDZKSO-UHFFFAOYSA-N propan-2-olate Chemical compound CC(C)[O-] OGHBATFHNDZKSO-UHFFFAOYSA-N 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 230000008707 rearrangement Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000003765 sweetening agent Substances 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- OVZUSPADPSOQQN-UHFFFAOYSA-N tri(propan-2-yloxy)indigane Chemical compound [In+3].CC(C)[O-].CC(C)[O-].CC(C)[O-] OVZUSPADPSOQQN-UHFFFAOYSA-N 0.000 description 1
- 238000004876 x-ray fluorescence Methods 0.000 description 1
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- C07H3/00—Compounds containing only hydrogen atoms and saccharide radicals having only carbon, hydrogen, and oxygen atoms
- C07H3/02—Monosaccharides
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- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/02—Boron or aluminium; Oxides or hydroxides thereof
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- 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
- B01J27/16—Phosphorus; Compounds thereof containing oxygen, i.e. acids, anhydrides and their derivates with N, S, B or halogens without carriers or on carriers based on C, Si, Al or Zr; also salts of Si, Al and Zr
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- B01J27/14—Phosphorus; Compounds thereof
- B01J27/16—Phosphorus; Compounds thereof containing oxygen, i.e. acids, anhydrides and their derivates with N, S, B or halogens without carriers or on carriers based on C, Si, Al or Zr; also salts of Si, Al and Zr
- B01J27/18—Phosphorus; Compounds thereof containing oxygen, i.e. acids, anhydrides and their derivates with N, S, B or halogens without carriers or on carriers based on C, Si, Al or Zr; also salts of Si, Al and Zr with metals other than Al or Zr
- B01J27/1802—Salts or mixtures of anhydrides with compounds of other metals than V, Nb, Ta, Cr, Mo, W, Mn, Tc, Re, e.g. phosphates, thiophosphates
- B01J27/1811—Salts or mixtures of anhydrides with compounds of other metals than V, Nb, Ta, Cr, Mo, W, Mn, Tc, Re, e.g. phosphates, thiophosphates with gallium, indium or thallium
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Abstract
Description
また、リン酸アルミニウムは、触媒活性が低いだけでなく、フルクトースの選択性が低く、工業触媒としての応用は難しい。
従って、本発明の課題は、水中又は水溶液中で目的とするグルコースからフルクトースへのヒドリド異性化反応を選択的に触媒できる新たな触媒を提供することにある。
〔2〕第13族元素酸化物が、酸化アルミニウム、酸化ガリウム、酸化インジウム及び酸化タリウムから選ばれるものである〔1〕記載の固体触媒。
〔3〕リン酸処理が、第13族元素酸化物をリン酸水溶液中50℃以下で処理するものである〔1〕又は〔2〕記載の固体触媒。
〔4〕表面がリン酸処理された第13族元素酸化物のルイス酸量が、その表面が水和された状態において、リン酸処理していない第13族元素酸化物の表面脱水物のルイス酸量の80%以上を維持しているものである〔1〕〜〔3〕のいずれかに記載の固体触媒。
〔5〕水中又は水溶液中でグリコースに〔1〕〜〔4〕のいずれかに記載の触媒を作用させることを特徴とするフルクトースの製造法。
これらの第13族元素酸化物のうち、酸化アルミニウムが入手容易性等の点で好ましい。
リン酸処理後は、濾過等により表面がリン酸処理された第13族元素酸化物を混合液から分離すればよい。
なお、表面がリン酸化された第13族元素酸化物は、表面を水和した場合、表面脱水物よりもルイス酸量が向上している。この作用により、この触媒は水中又は水溶液中において優れたヒドリド異性化反応を触媒するものと考えられる。
水中又は水溶液中でグルコースに本発明触媒を作用させると、副反応が抑制され、ヒドリド異性化反応が選択的に進行し、フルクトースを選択的に製造することができる。
アルミニウムイソプロポキシド(Al(O−i−Pr)3)30gに水300mLを加え、80℃で5時間攪拌した後、放冷し、水を除去した。この前駆体を200〜1100℃で3時間焼成し、酸化アルミニウム粉末を得た。得られた酸化アルミニウムのX線回折スペクトル(XRD)を図1に、BET比表面積及びXRDによる結晶相を表1に示す。表中のAl−200〜Al−1100は、それぞれ200〜1100℃の焼成温度で得られた酸化アルミニウムを示す。
ガリウムイソプロポキシド(Ga(O−i−Pro)3)又はインジウムイソプロポキシド(In(O−i−Pro)3)3〜5gに、2−プロパノール75〜100mL、酢酸0.02〜0.1mL及び水0.1〜1.0mLを加え、80℃で5時間攪拌し、濾過後乾燥した。得られた前駆体を200〜1000℃で3時間焼成し、Ga2O3又はIn2O3を得た。得られた生成物のBET比表面積を表2に示す。表2中、Ga2O3又はIn2O3の数字は焼成温度を示す。
(1)参考例1で製造した酸化アルミニウム5gを0.1Mリン酸水溶液200mL中、25℃で24時間攪拌した。濾過後、乾燥し、リン酸処理酸化アルミニウム5.1gを得た。X線蛍光分析から、リン酸を5質量%含有することがわかる。
図3から計算されたルイス酸量を表3に示す。
参考例2で製造した酸化ガリウム又は酸化インジウム5gを0.1Mリン酸水溶液200mL中、25℃で24時間攪拌した。濾過後、乾燥し、リン酸処理酸化ガリウム又はリン酸処理酸化インジウム4.5gを得た。
グルコース0.02g、水2g及びリン酸処理酸化アルミニウム0.05gを反応容器に入れ、120℃で2時間攪拌した。反応液を高速液体クロマトグラフィーにより分析した。その結果を図4に示す。なお、図4には、触媒としてリン酸処理していない酸化アルミニウムを用いた場合の結果も示した。図中、Alは酸化アルミニウムを示し、その後ろの数字は焼成温度を示す。0.1MPPは0.1Mリン酸処理を示す。
1質量%グルコース水溶液にリン酸処理酸化アルミニウム(600℃で焼成した酸化アルミニウムを10〜100mMのリン酸水溶液で、25℃、1〜24時間攪拌)0.05gを添加し、120℃で2時間攪拌した。反応液を高速液体クロマトグラフィーにより分析した。その結果を図6に示す。図中、PP−Al2O3のかっこ内の記載はリン酸処理の条件を示す。図中、選択率はフルクトースの選択率を示す。
グルコースの反応温度を120℃から100℃に変化させる以外は、実施例4と同様に反応を行った。その結果を図7に示す。図中の記号、選択率は図6と同じである。なお、図中の*の試料は、グルコースの反応時間が6時間である。
1質量%グルコース水溶液(2mL)に酸化ガリウムと酸化インジウム(400℃焼成した試料)とそのリン酸処理物(試料を100mMのリン酸水溶液で、25℃、48時間攪拌)0.05gを添加し、120℃で2時間攪拌した。反応液を高速液体クロマトグラフィーにより分析した。その結果を表4に示す。
Claims (5)
- 表面がリン酸処理された第13族元素酸化物からなる水中又は水溶液中におけるグルコースからフルクトースへのヒドリド異性化反応用固体触媒。
- 第13族元素酸化物が、酸化アルミニウム、酸化ガリウム、酸化インジウム及び酸化タリウムから選ばれるものである請求項1記載の固体触媒。
- リン酸処理が、第13族元素酸化物をリン酸水溶液中50℃以下で処理するものである請求項1又は2記載の固体触媒。
- 表面がリン酸処理された第13族元素酸化物のルイス酸量が、その表面が水和された状態において、リン酸処理していない第13族元素酸化物の表面脱水物のルイス酸量の80%以上を維持しているものである請求項1〜3のいずれか1項記載の固体触媒。
- 水中又は水溶液中でグルコースに請求項1〜4のいずれか1項記載の固体触媒を作用させることを特徴とするフルクトースの製造法。
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JP2007196174A (ja) * | 2006-01-28 | 2007-08-09 | Osaka Industrial Promotion Organization | 不均一系リン酸ジルコニウム触媒、脱水反応方法、5−ヒドロキシメチルフルフラール製造方法、セルロース分解方法、及び不均一系リン酸ジルコニウム触媒の再生方法 |
WO2012108472A1 (ja) * | 2011-02-08 | 2012-08-16 | 財団法人神奈川科学技術アカデミー | アモルファス含水チタン酸化物及びそれを含む固体ルイス酸触媒 |
JP2013006142A (ja) * | 2011-06-23 | 2013-01-10 | Toshiba Corp | 植物系材料の加水分解用触媒及び糖類の製造方法 |
WO2013030132A1 (fr) * | 2011-08-26 | 2013-03-07 | Centre National De La Recherche Scientifique (C.N.R.S) | Procede d'isomerisation du glucose en fructose |
JP2013517288A (ja) * | 2010-01-15 | 2013-05-16 | カリフォルニア インスティチュート オブ テクノロジー | 糖の異性化 |
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US5139759A (en) * | 1991-12-19 | 1992-08-18 | Uop | Synthesis of zeolite beta |
DE4238493C1 (de) * | 1992-11-14 | 1994-04-21 | Degussa | Verfahren zur Herstellung von Acrolein und dessen Verwendung |
US5985790A (en) * | 1994-12-07 | 1999-11-16 | Project Earth Industries, Inc. | Method of making acid contacted enhanced aluminum oxide adsorbent particle |
CN1228036A (zh) * | 1996-06-12 | 1999-09-08 | 计划地球工业公司 | 酸接触增强的吸附剂和/或催化剂和粘合剂系统 |
US6034017A (en) | 1998-04-06 | 2000-03-07 | Coastal Catalyst Technology, Inc. | Use of phosphrous to enhance the acid sites of FCC catalysts |
KR100461758B1 (ko) * | 2002-09-16 | 2004-12-14 | 한국화학연구원 | 폐가스 중의 과불화화합물 분해제거용 촉매와 이를 이용한폐가스중의 과불화화합물 분해제거 방법 |
US7916700B2 (en) * | 2004-06-30 | 2011-03-29 | Nokia Corporation | Dynamic service information for the access network |
FR2882053B1 (fr) * | 2005-02-15 | 2007-03-23 | Arkema Sa | Procede de deshydratation du glycerol en acrolene |
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JP5635752B2 (ja) * | 2009-09-25 | 2014-12-03 | 日本ケッチェン株式会社 | 水素化処理触媒の製造方法、並びに当該触媒を用いる炭化水素油の水素化処理方法 |
ES2581324T5 (es) * | 2010-01-15 | 2019-11-28 | California Inst Of Techn | Isomerización de azúcares |
US8642791B2 (en) * | 2011-12-07 | 2014-02-04 | Wisconsin Alumni Research Foundation | Lewis and bronsted-lowry acid-catalyzed production 5-hydroxymethylfurfural (HMF) from glucose |
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JP2007196174A (ja) * | 2006-01-28 | 2007-08-09 | Osaka Industrial Promotion Organization | 不均一系リン酸ジルコニウム触媒、脱水反応方法、5−ヒドロキシメチルフルフラール製造方法、セルロース分解方法、及び不均一系リン酸ジルコニウム触媒の再生方法 |
JP2013517288A (ja) * | 2010-01-15 | 2013-05-16 | カリフォルニア インスティチュート オブ テクノロジー | 糖の異性化 |
WO2012108472A1 (ja) * | 2011-02-08 | 2012-08-16 | 財団法人神奈川科学技術アカデミー | アモルファス含水チタン酸化物及びそれを含む固体ルイス酸触媒 |
JP2013006142A (ja) * | 2011-06-23 | 2013-01-10 | Toshiba Corp | 植物系材料の加水分解用触媒及び糖類の製造方法 |
WO2013030132A1 (fr) * | 2011-08-26 | 2013-03-07 | Centre National De La Recherche Scientifique (C.N.R.S) | Procede d'isomerisation du glucose en fructose |
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WO2015137339A1 (ja) | 2015-09-17 |
CN106102907A (zh) | 2016-11-09 |
CN106102907B (zh) | 2019-05-10 |
EP3117902A1 (en) | 2017-01-18 |
US20170022238A1 (en) | 2017-01-26 |
JP6444986B2 (ja) | 2018-12-26 |
EP3117902A4 (en) | 2017-11-15 |
US10336783B2 (en) | 2019-07-02 |
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