KR920006032A - 철-안티몬-몰리브덴-함유 산화물 촉매 조성물 및 이의 제조 방법 - Google Patents

철-안티몬-몰리브덴-함유 산화물 촉매 조성물 및 이의 제조 방법 Download PDF

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KR920006032A
KR920006032A KR1019910015664A KR910015664A KR920006032A KR 920006032 A KR920006032 A KR 920006032A KR 1019910015664 A KR1019910015664 A KR 1019910015664A KR 910015664 A KR910015664 A KR 910015664A KR 920006032 A KR920006032 A KR 920006032A
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aqueous slurry
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유타카 사사키
히로시 야마모토
고이치 미주타니
기요시 모리야
구니오 모리
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닛토가가쿠고교 가부시키가이샤
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Abstract

내용 없음

Description

철-안티몬-몰리브덴-함유 산화물 촉매 조성물 및 이의 제조방법
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음

Claims (12)

  1. 미소결정 크기가 100Å 이상인 결정성 안티몬산 철을 포함하는, 하기 실험식으로 표시되는 산화 반응용 철-안티몬-몰리브덴-함유 산화물 촉매 조성물.
    FeaSbbMocLdKeMmNnQgRrTtOx
    상기식에서, L은 Bi 및 Te로 이루어진 그룹중에서 선택된 원소 하나이상을 나타내고, M은 Cu,Mg,Zn,La,Ce,Al,Cr,Mn,Co,Ni 및 Sn으로 이루어진 그룹중에서 선택된 원소 하나 이상을 나타내며, Be, Ca, Sr, Ba, Y, Pr, Nd, Th, U, Ti, Zr, Hf, Nb, Ta, Re, Ru, Os, Rh, Ir, Pd, Pt, Ag, Au, Cd, Al, Ga, In, Ge 및 Pd로 이루어진 그룹중에서 선택된 원소 하나 이상을 나타내고, Q는 V 및 W로 이루어진 그룹중에서 선택된 원소 하나 이상을 나타내며; R은 Li,Na,Se로 이루어진 그룹중에서 선택된 원소 하나 이상을 나타내며, T는 B,P,As 및 Rb,Cs 및 Ti로 이루어진 그룹중에서 선택된 원소 하나 이상을 나타내며, a,b,c,d,e,n,q,r,t 및 X는 각각, 원자비를 나타내며 a는 10이고 b는 5 내지 30이고, d는 0.01 내지 10이며, e는 0.01 내지 5이고, m은 0 내지 300이며, n은 0 내지 10이고, q는 0 내지 5이며, r은 0 내지 3이고, t는 0 내지 5이며, x는 상기에 언급한 성분들을 합하여 제조한 산화물에 상응하는 측정된 산소 원자의 수를 나타낸다.
  2. 제1항에 있어서, 촉매중의 안티몬산철의 미소결정 크기가 200Å 미만인 촉매 조성물.
  3. 제1항에 있어서, M이 Zn, Ce, Cr, Mn, Co 및 Ni로 이루어진 그룹중에서 선택된 하나 이상의 원소이고, N이 Ti, Zr, Nb, Pd, Ag, Ge 및 Pb로 이루어진 그룹중에서 선택된 하나 이상의 원소이며, R이 Li, Na 및 Cs로 이루어진 그룹중에서 선택된 하나 이상의 원소이고, T가 B 및/또는 P인 촉매 조성물.
  4. 제1항에 있어서, 촉매 조성물중의 성분들의 비를 나타내는 a가 10이고, b가 6 내지 30이며, c가 6 내지 20이고, d가 0.1 내지 8이며, e가 0.02 내지 2이고, m은 0 내지 20이며, n은 0 내지 5이고, q는 0 내지 4이며, r은 0 내지 2.5이고 t가 0 내지 4인 촉매 조성물.
  5. 제1항에 있어서, T성분으로서 P를 사용하고, P/Fe의 원자비가 0.3이하인 촉매 조성물.
  6. 제1항에 있어서, 산화물 촉매를 담체상에 지지시킨 촉매 조성물.
  7. 주성분으로 (ⅰ) 안티몬산철, (ⅱ) 몰리브덴, (ⅲ) 비스무트 및 텔루륨으로 이루어진 그룹중에서 선택된 원소 하나 이상, 및 (ⅳ) 칼륨을 함유하는 수성 슬러리, 또는 상기한 주성분[(ⅰ),(ⅱ),(ⅲ) 및 (ⅳ)] 및 (ⅴ) 실험식에서 M,N,Q,R 및 T로서 표시된 촉매 성분으로 이루어진 그룹중에서 선택된 원소 하나 이상을 함유하는 수성 슬러리를 제조하고; 수성 슬러리를 건조시킨 다음; 건조된 생성물을 하소시키는 단계들을 포함하여, 미소 결정 크기가 100Å이상인 결정성 안티몬산철을 포함하는, 하기 실험식으로 표시되는 산화 반응용 철-안티몬-몰리브덴-함유 산화물 촉매 조성물을 제조하는 방법.
    FeaSbbMocLdKeMmNnQgRrTtOx
    상기식에서, L은 Bi 및 Te로 이루어진 그룹중에서 선택된 원소 하나이상을 나타내고, M은 Cu,Mg,Zn,La,Ce,Al,Cr,Mn,Co,Ni 및 Sn으로 이루어진 그룹중에서 선택된 원소 하나 이상을 나타내며, N은 Be, Ca, Sr, Ba, Y, Pr, Nd, Th, U, Ti, Zr, Hf, Nb, Ta, Re, Ru, Os, Rh, Ir, Pd, Pt, Ag, Au, Cd, Al, ga, In, Ge 및 Pd로 이루어진 그룹중에서 선택된 원소 하나 이상을 나타내고, Q는 V 및 W로 이루어진 그룹중에서 선택된 원소 하나 이상을 나타내며; R은 Li, Na, Rb, Cs및 TI로 이루어진 그룹중에서 선택된원소 하나이상을 나타내고, T는 B,P,As 및 Se로 이루어진 그룹중에서 선택된 원소 하나 이상을 나타내고, a,b,c,d,e,m,n,q,r,t 및 X는 각각, 원자비를 나타내며 a는 10이고 b는 5 내지 60이며, c는 5 내지 30이고, d는 0.01 내지 10이며, e는 0.01 내지 5이고, m은 0 내지 30이며, n은 0 내지 10이고, q는 0 내지 5이며, r은 0 내지 3이고, t는 0 내지 5이면, x는 상기에 언급한 성분들을 합하여 제조한 산화물에 상응하는 측정된 산소 원자의 수를 나타낸다.
  8. 제7항에 있어서, 수성 슬러리가 담체 성분용 원료 물질을 함유하는 방법.
  9. 제7항에 있어서, 수성 슬러리의 pH를 5이하로 조절하는 방법.
  10. 제7항에 있어서, 수성 슬러리의 pH를 7이상으로 조절하는 방법.
  11. 제7항에 있어서, 수성 슬러리의 pH를 6이상으로 조절하고 수성 슬러리가 킬레이트제를 함유하는 방법.
  12. 제7항에 있어서, 수성 슬러리의 pH를 6이상으로 조절하고 수성 슬러리가 킬레이트제 및 철 킬레이트 화합물을 함유하는 방법.
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019910015664A 1990-09-10 1991-09-09 철-안티몬-몰리브덴함유 산화물 촉매 조성물 및 이의 제조방법 KR100191368B1 (ko)

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JP02237002A JP3142549B2 (ja) 1990-09-10 1990-09-10 鉄・アンチモン・モリブデン含有酸化物触媒組成物およびその製法

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Families Citing this family (66)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19519008A1 (de) * 1995-05-24 1996-11-28 Hoechst Ag Neue ruthenium- und selen- oder schwefelhaltige Metalloxidkatalysatoren sowie ein Verfahren zu ihrer Herstellung und ihre Verwendung
DE19519004A1 (de) * 1995-05-24 1996-11-28 Hoechst Ag Neue selen- und rutheniumhaltige Metalloxidkatalysatoren sowie ein Verfahren zu ihrer Herstellung und ihre Verwendung
JP3982852B2 (ja) * 1995-06-30 2007-09-26 三菱レイヨン株式会社 流動層プロセス
KR100204729B1 (ko) * 1997-03-17 1999-06-15 성재갑 아크롤레인 부분산화용 촉매의 제조 방법
US5840648A (en) * 1997-09-02 1998-11-24 The Standard Oil Company Catalyst for the manufacture of acrylonitrile and hydrogen cyanide
US6924387B1 (en) * 1998-02-13 2005-08-02 Korea Research Institute Of Chemical Technology Solid catalyst with core-shell catalytic phase and a method of preparation thereof
CN1155439C (zh) 1998-04-23 2004-06-30 三菱丽阳株式会社 用于生产不饱和腈类的催化剂
WO1999054037A1 (fr) * 1998-04-23 1999-10-28 Mitsubishi Rayon Co., Ltd. Catalyseur de production de nitrile insature
JP3573959B2 (ja) 1998-05-12 2004-10-06 ダイヤニトリックス株式会社 モリブデン含有酸化物流動層触媒の再生法
US6632772B2 (en) 1998-09-23 2003-10-14 Lg Chemical, Ltd. Method of coating a catalyst to a support for use in acrolein oxidation
US6060421A (en) * 1998-12-23 2000-05-09 Saudi Basic Industries Corporation Catalysts for the oxidation of ethane to acetic acid, methods of making and using the same
US6037304A (en) * 1999-01-11 2000-03-14 Saudi Basic Industries Corporation Highly active and selective catalysts for the production of unsaturated nitriles, methods of making and using the same
US6017846A (en) * 1999-01-11 2000-01-25 Saudi Basic Industries Corporation Highly active and selective catalysts for the production of unsaturated nitriles, methods of making and using the same
US6417422B1 (en) 1999-02-22 2002-07-09 Symyx Technologies, Inc. Ni catalysts and methods for alkane dehydrogenation
US6355854B1 (en) 1999-02-22 2002-03-12 Symyx Technologies, Inc. Processes for oxidative dehydrogenation
US6436871B1 (en) * 1999-02-22 2002-08-20 Symyx Technologies, Inc. Catalysts for oxidative dehydrogenation
WO2000072962A1 (en) * 1999-05-27 2000-12-07 Solutia Inc. Process for improving activity and selectivity of ammoxidation catalyst
JP2001029788A (ja) * 1999-07-21 2001-02-06 Mitsubishi Rayon Co Ltd モリブデン−ビスマス−鉄含有金属酸化物流動層触媒の製法
JP3819192B2 (ja) 1999-10-18 2006-09-06 ダイヤニトリックス株式会社 アクリロニトリルの製造法
RO121264B1 (ro) 1999-10-18 2007-02-28 Mitsubishi Rayon Co., Ltd. Procedeu pentru producerea acrilonitrilului, catalizator utilizabil în acest procedeu şi procedeupentru prepararea acestuia
US6486091B1 (en) 2000-03-14 2002-11-26 Saudi Basic Industries Corporation Process for making highly active and selective catalysts for the production of unsaturated nitriles
US6337424B1 (en) * 2000-04-28 2002-01-08 Saudi Basic Industries Corporation Catalysts oxidation of lower olefins to unsaturated aldehydes, methods of making and using the same
US6588966B2 (en) * 2000-09-15 2003-07-08 Quantum Engineering, Inc. End of train coupler mounting device
JP4666334B2 (ja) * 2000-09-18 2011-04-06 旭化成ケミカルズ株式会社 酸化又はアンモ酸化用酸化物触媒の製造方法
US6734136B2 (en) 2000-09-28 2004-05-11 Rohm And Haas Company IR and/or SM promoted multi-metal oxide catalyst
US6677497B2 (en) 2001-03-22 2004-01-13 Symyx Technologies, Inc. Ni catalysts and methods for alkane dehydrogenation
JP4159759B2 (ja) * 2001-04-13 2008-10-01 ダイヤニトリックス株式会社 モリブデン−ビスマス−鉄含有複合酸化物流動層触媒の製法
JP4030740B2 (ja) * 2001-10-11 2008-01-09 ダイヤニトリックス株式会社 アンモ酸化用触媒の製造方法
WO2003039744A1 (fr) * 2001-11-08 2003-05-15 Mitsubishi Chemical Corporation Catalyseur a base d'oxyde composite et son procede de preparation
JP4242197B2 (ja) * 2003-04-18 2009-03-18 ダイヤニトリックス株式会社 アクリロニトリル合成用触媒
JP4503315B2 (ja) * 2004-03-09 2010-07-14 ダイヤニトリックス株式会社 鉄・アンチモン・テルル含有金属酸化物触媒の製造方法
KR101183773B1 (ko) 2005-02-18 2012-09-17 미츠비시 레이온 가부시키가이샤 팔라듐 함유 촉매, 그 제조 방법 및 α,β-불포화카르복실산의 제조 방법
US7851397B2 (en) 2005-07-25 2010-12-14 Saudi Basic Industries Corporation Catalyst for methacrolein oxidation and method for making and using same
US7649111B2 (en) 2005-07-25 2010-01-19 Saudi Basic Industries Corporation Catalyst for the oxidation of a mixed aldehyde feedstock to methacrylic acid and methods for making and using same
US7649112B2 (en) 2005-07-25 2010-01-19 Saudi Basic Industries Corporation Integrated plant for producing 2-ethyl-hexanol and methacrylic acid and a method based thereon
US7732367B2 (en) 2005-07-25 2010-06-08 Saudi Basic Industries Corporation Catalyst for methacrolein oxidation and method for making and using same
KR100807972B1 (ko) 2005-08-10 2008-02-28 주식회사 엘지화학 아크릴산 선택성이 높은 복합 금속 산화물 촉매
WO2007034264A1 (en) * 2005-09-20 2007-03-29 Arkema France Process for preparing partial oxidation products of lower alcohols by direct oxidation of a lower alcohol and catalysts for use in that process
JP4902991B2 (ja) * 2005-12-27 2012-03-21 三菱レイヨン株式会社 酸化物触媒の製造方法
FR2912742B1 (fr) * 2007-02-16 2010-03-05 Arkema France Procede de synthese d'acrylonitrile a partir de glycerol
CA2685692A1 (en) * 2007-05-03 2008-11-13 Shell Internationale Research Maatschappij B.V. A catalyst, its preparation and use
CN101422735B (zh) * 2007-11-01 2010-12-15 中国石油天然气股份有限公司 一种乙苯脱氢制苯乙烯的催化剂及其制备方法
JP5011176B2 (ja) 2008-03-14 2012-08-29 ダイヤニトリックス株式会社 アクリロニトリル合成用触媒およびアクリロニトリルの製造方法
CN101579631A (zh) * 2009-06-22 2009-11-18 上海华谊丙烯酸有限公司 一种用于低碳烯烃选择氧化制备不饱和醛反应的催化剂的制备方法
JP5560642B2 (ja) 2009-10-09 2014-07-30 三菱レイヨン株式会社 複合酸化物触媒の製造方法
JP5663902B2 (ja) * 2010-03-05 2015-02-04 三菱レイヨン株式会社 メタクリル酸製造用触媒の製造方法
JP5609254B2 (ja) * 2010-05-14 2014-10-22 三菱レイヨン株式会社 複合酸化物触媒の製造方法
JP5710749B2 (ja) * 2011-04-21 2015-04-30 旭化成ケミカルズ株式会社 シリカ担持触媒
US8921257B2 (en) 2011-12-02 2014-12-30 Saudi Basic Industries Corporation Dual function partial oxidation catalyst for propane to acrylic acid conversion
US9181178B2 (en) 2012-02-29 2015-11-10 Mitsubishi Rayon Co., Ltd. Method for producing acrylonitrile
WO2013129363A1 (ja) 2012-02-29 2013-09-06 三菱レイヨン株式会社 アクリロニトリルの製造方法
CN104203908B (zh) 2012-02-29 2016-12-07 三菱丽阳株式会社 丙烯腈的制造方法
US8722940B2 (en) 2012-03-01 2014-05-13 Saudi Basic Industries Corporation High molybdenum mixed metal oxide catalysts for the production of unsaturated aldehydes from olefins
CN104994945A (zh) * 2013-02-21 2015-10-21 三菱丽阳株式会社 丙烯腈制造用催化剂和丙烯腈的制造方法
WO2014129566A1 (ja) * 2013-02-25 2014-08-28 三菱レイヨン株式会社 アクリロニトリル製造用触媒の製造方法およびアクリロニトリルの製造方法
WO2014167482A1 (en) 2013-04-08 2014-10-16 Saudi Basic Industries Corporation Catalyst for conversion of propylene to product comprising a carboxylic acid moiety
KR101507686B1 (ko) 2013-05-06 2015-03-31 주식회사 엘지화학 메조포러스 복합 산화물 촉매, 그 제조방법 및 이를 이용한 1,3­부타디엔 합성방법
KR101495478B1 (ko) 2013-05-06 2015-02-23 주식회사 엘지화학 부타디엔 제조를 위한 산화촉매 및 그 제조방법
CN104284721B (zh) * 2013-05-06 2017-09-05 Lg化学株式会社 用于生产丁二烯的氧化催化剂及其制备方法
WO2017120566A1 (en) * 2016-01-09 2017-07-13 Ascend Performance Materials Operations Llc Catalyst compositions and process for direct production of hydrogen cyanide in an acrylonitrile reactor feed stream
CN107684927B (zh) * 2016-08-03 2020-07-28 万华化学集团股份有限公司 一种用于氯化氢氧化制备氯气的催化剂及其制备方法和用途
RU2709012C1 (ru) * 2016-08-31 2019-12-13 Асахи Касеи Кабусики Кайся Способ получения катализатора и способ получения акрилонитрила
JP6467115B2 (ja) * 2016-08-31 2019-02-06 旭化成株式会社 触媒の製造方法、及びアクリロニトリルの製造方法
JP6914114B2 (ja) * 2017-06-23 2021-08-04 旭化成株式会社 金属酸化物触媒及びその製造方法ならびにそれを用いたアクリロニトリルの製造方法
CN114100652B (zh) * 2021-12-10 2023-10-13 北京道思克矿山装备技术有限公司 一种甲醇气相催化氨氧化生产氰化氢的催化剂及其制备方法和应用
CN115555025B (zh) * 2022-10-31 2024-01-26 河北建材职业技术学院 一种高分散钴钼双金属催化剂的制备方法

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4111984A (en) * 1973-06-11 1978-09-05 Mitsubishi Rayon Co., Ltd. Process for producing unsaturated aldehydes, and unsaturated fatty acids
US4018712A (en) * 1973-12-27 1977-04-19 Monsanto Company Oxidation/ammoxidation catalyst
JPS5318014B2 (ko) * 1974-02-09 1978-06-13
US4306090A (en) * 1979-10-12 1981-12-15 Rohm And Haas Company Catalyst compositions and their use for the preparation of methacrolein
US4290920A (en) * 1979-12-28 1981-09-22 The Standard Oil Co. Sb-containing catalysts by Sb-oxide impregnation
JPS63122642A (ja) * 1986-11-11 1988-05-26 Mitsubishi Rayon Co Ltd メタクロレイン及びメタクリル酸の製造法
JPH0763629B2 (ja) * 1987-12-25 1995-07-12 日東化学工業株式会社 流動層反応に適する鉄・アンチモン・リン含有触媒の製法
JPH0764555B2 (ja) * 1988-04-05 1995-07-12 日東化学工業株式会社 青酸製法
JP2747920B2 (ja) * 1989-02-16 1998-05-06 日東化学工業株式会社 酸化反応に適するモリブデン含有金属酸化物流動層触媒の製法

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EP0475351A1 (en) 1992-03-18
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US5132269A (en) 1992-07-21
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