AR008101A1 - Procedimiento para la preparacion selectiva de acido acetico a partir de un material gaseoso de alimentación y un catalizador para su exclusivo uso en dicho procedimiento - Google Patents

Procedimiento para la preparacion selectiva de acido acetico a partir de un material gaseoso de alimentación y un catalizador para su exclusivo uso en dicho procedimiento

Info

Publication number
AR008101A1
AR008101A1 ARP970103425A ARP970103425A AR008101A1 AR 008101 A1 AR008101 A1 AR 008101A1 AR P970103425 A ARP970103425 A AR P970103425A AR P970103425 A ARP970103425 A AR P970103425A AR 008101 A1 AR008101 A1 AR 008101A1
Authority
AR
Argentina
Prior art keywords
procedure
catalyst
acetic acid
exclusive use
selective preparation
Prior art date
Application number
ARP970103425A
Other languages
English (en)
Original Assignee
Celanese Gmbh
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Celanese Gmbh filed Critical Celanese Gmbh
Publication of AR008101A1 publication Critical patent/AR008101A1/es

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/16Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
    • C07C51/21Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
    • C07C51/215Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of saturated hydrocarbyl groups
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/54Catalysts 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
    • B01J23/56Platinum group metals
    • B01J23/64Platinum group metals with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/652Chromium, molybdenum or tungsten
    • B01J23/6525Molybdenum
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/16Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
    • C07C51/21Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
    • C07C51/25Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)

Abstract

Procedimiento para la preparación selectiva de ácido acético a partir de un material gaseoso de alimentación, constituido por etano, etileno o mezclas deellos así como oxígeno, a temperatura elevada, en el cual el material gaseoso de alimentacióne s reunido con un catalizador, que contiene los elementos Mo,Pd, X e Y en las relaciones, expresadas en átomos-gramo a:b:c:d en combinación con oxígeno: Mo(a)Pd(b)X(c)Y(d) (I) teniendo los símbolos X e Y los siguientessignificados: X representauno d e varios elementos que se seleccionan entre el grupo formado por: Cr, Mn, Nb, Ta, Ti, V, Te y/o W; Y representa uno ovarios de los elementos que se seleccionan entre el grupo formado por: B, Al, Ga, In, Pt, Zn, Cd, Bi, Ce, Co, Rh, Ir,Cu, Ag, A u, Fe, Ru, Os, K, Rb, Cs, Mg,Ca, Sr, Ba, Zr, Hf, Ni, P, Pb, Sb, Si, Sn, TI y U; los índices a, b, c, d y x representan las relaciones, expresadas en átomos-gramo, de los correspondienteselementos, siendo a=1, b>0, c>0 y d=0-2 y elcatalizador de fó rmula (I) para su exclusivo uso en dicho procedimiento
ARP970103425A 1996-07-31 1997-07-29 Procedimiento para la preparacion selectiva de acido acetico a partir de un material gaseoso de alimentación y un catalizador para su exclusivo uso en dicho procedimiento AR008101A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19630832A DE19630832A1 (de) 1996-07-31 1996-07-31 Verfahren zur selektiven Herstellung von Essigsäure

Publications (1)

Publication Number Publication Date
AR008101A1 true AR008101A1 (es) 1999-12-09

Family

ID=7801332

Family Applications (2)

Application Number Title Priority Date Filing Date
ARP970103425A AR008101A1 (es) 1996-07-31 1997-07-29 Procedimiento para la preparacion selectiva de acido acetico a partir de un material gaseoso de alimentación y un catalizador para su exclusivo uso en dicho procedimiento
ARP040103517A AR045953A2 (es) 1996-07-31 2004-09-28 Catalizador para la oxidacion selectiva de etano o mezclas de etano y etileno mas oxigeno

Family Applications After (1)

Application Number Title Priority Date Filing Date
ARP040103517A AR045953A2 (es) 1996-07-31 2004-09-28 Catalizador para la oxidacion selectiva de etano o mezclas de etano y etileno mas oxigeno

Country Status (28)

Country Link
US (2) US6194610B1 (es)
EP (1) EP0915821B1 (es)
JP (1) JP3992112B2 (es)
KR (1) KR100554189B1 (es)
CN (1) CN100360493C (es)
AR (2) AR008101A1 (es)
AT (1) ATE209175T1 (es)
AU (1) AU716609B2 (es)
BG (1) BG103119A (es)
BR (1) BR9710906B1 (es)
CA (1) CA2261894C (es)
CZ (1) CZ294658B6 (es)
DE (2) DE19630832A1 (es)
DK (1) DK0915821T3 (es)
ES (1) ES2167781T3 (es)
ID (1) ID18000A (es)
MY (1) MY120427A (es)
NO (1) NO323890B1 (es)
NZ (1) NZ333950A (es)
PL (1) PL188010B1 (es)
RS (1) RS49592B (es)
RU (1) RU2198869C2 (es)
SI (1) SI9720051A (es)
TR (1) TR199900162T2 (es)
TW (1) TW427971B (es)
UA (1) UA55420C2 (es)
WO (1) WO1998005619A1 (es)
ZA (1) ZA976793B (es)

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DE19745902A1 (de) 1997-10-17 1999-04-22 Hoechst Ag Verfahren zur selektiven Herstellung von Essigsäure durch katalytische Oxidation von Ethan
US6030920A (en) * 1997-12-24 2000-02-29 Saudi Basic Industries Corporation Catalysts for producing acetic acid from ethane oxidation, processes of making same and method of using same
GB9807142D0 (en) 1998-04-02 1998-06-03 Bp Chem Int Ltd Catalyst and process utilising the catalyst
US6087297A (en) * 1998-06-29 2000-07-11 Saudi Basic Industries Corporation Catalysts for gas phase production of acetic acid from ethane, processes of making the same and methods of using same
US6028221A (en) * 1998-06-29 2000-02-22 Saudi Basic Industries Corporation Catalyst systems for the one step gas phase production of acetic acid from ethylene and methods of making and using the same
GB9819221D0 (en) * 1998-09-04 1998-10-28 Bp Chem Int Ltd Process for the production of acetic acid
US6114278A (en) 1998-11-16 2000-09-05 Saudi Basic Industries Corporation Catalysts for catalytic oxidation of propane to acrylic acid, methods of making and using the same
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
GB9907704D0 (en) 1999-04-01 1999-05-26 Bp Chem Int Ltd Catalyst and process utilising the catalyst
US6143921A (en) 1999-05-14 2000-11-07 Saudi Basic Industries Corporation Method for producing vinyl acetate monomer from ethane or ethylene oxidation
JP4809532B2 (ja) * 1999-11-15 2011-11-09 サウディ ベーシック インダストリーズ コーポレイション プロパンのアクリル酸への接触酸化用触媒、その製造法及び使用法
US6531631B1 (en) 2000-04-28 2003-03-11 Saudi Basic Industries Corporation Oxidation of ethane to acetic acid and ethylene using molybdenum and vanadium based catalysts
US6441227B1 (en) * 2000-06-23 2002-08-27 Saudi Basic Industries Corporation Two stage process for the production of unsaturated carboxylic acids by oxidation of lower unsaturated hydrocarbons
DE10055810A1 (de) 2000-11-10 2002-05-23 Aventis Res & Tech Gmbh & Co Verfahren zur Herstellung von Essigsäure
US6841699B2 (en) * 2001-04-25 2005-01-11 Rohm And Haas Company Recalcined catalyst
EP1306129A1 (en) 2001-10-26 2003-05-02 Rohm And Haas Company Preparation of a mixed metal oxide catalyst and its use in oxidation and ammoxidation reactions
US6919295B2 (en) * 2002-05-01 2005-07-19 Rohm And Haas Company Supported mixed metal oxide catalyst
UA79540C2 (uk) 2003-01-27 2007-06-25 Бп Кемікалз Лімітед Каталітична композиція окиснення, її одержання та спосіб селективного окиснення
KR100806263B1 (ko) * 2004-03-29 2008-02-22 쇼와 덴코 가부시키가이샤 산소 함유 화합물 제조용 팔라듐, 텅스텐 및 지르코늄계촉매, 그 촉매의 제조 방법, 및 그 촉매를 사용한 산소함유 화합물의 제조 방법
CN101421038B (zh) * 2006-02-07 2013-02-13 国际人造丝公司 在生产乙酸的乙烷基方法中使用化学反应将乙烯和乙烷分离
JP5305699B2 (ja) * 2007-03-19 2013-10-02 株式会社東芝 触媒、触媒の製造方法、膜電極複合体及び燃料電池
KR20100017604A (ko) * 2007-05-04 2010-02-16 비피 코포레이션 노쓰 아메리카 인코포레이티드 방향족 화합물의 산화를 위한 방법 및 촉매
WO2008136857A1 (en) * 2007-05-04 2008-11-13 Bp Corporation North America Inc. Process for the production of non-aromatic carboxylic acids
CN101058072B (zh) * 2007-05-16 2010-06-23 天津兴新催化反应技术研究与开发有限责任公司 Co和h2直接合成乙烯催化剂及其工艺
CN102056661A (zh) * 2008-06-10 2011-05-11 Lg化学株式会社 烃的气相接触氧化催化剂、其制备方法以及使用该催化剂的烃的气相氧化方法
WO2009151255A2 (en) * 2008-06-10 2009-12-17 Lg Chem, Ltd. Catalyst for gas-phase contact oxidation of hydrocarbon, preparation method thereof and gas-phase oxidation method of hydrocarbon using the same
US8105972B2 (en) * 2009-04-02 2012-01-31 Lummus Technology Inc. Catalysts for the conversion of paraffins to olefins and use thereof
US8105971B2 (en) * 2009-04-02 2012-01-31 Lummus Technology Inc. Process for making catalysts useful for the conversion of paraffins to olefins
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CN112703055A (zh) 2018-09-17 2021-04-23 沙特基础工业全球技术公司 选择性氧化催化剂和在选择性氧化催化剂的存在下氧化c2烃的方法

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Also Published As

Publication number Publication date
EP0915821A1 (de) 1999-05-19
TR199900162T2 (xx) 1999-03-22
TW427971B (en) 2001-04-01
PL331374A1 (en) 1999-07-05
AR045953A2 (es) 2005-11-16
US6194610B1 (en) 2001-02-27
CZ294658B6 (cs) 2005-02-16
CN1231656A (zh) 1999-10-13
YU4099A (sh) 1999-12-27
DE19630832A1 (de) 1998-02-05
CA2261894A1 (en) 1998-02-12
RU2198869C2 (ru) 2003-02-20
AU716609B2 (en) 2000-03-02
JP2000515158A (ja) 2000-11-14
DK0915821T3 (da) 2002-05-21
KR20000035787A (ko) 2000-06-26
KR100554189B1 (ko) 2006-02-22
JP3992112B2 (ja) 2007-10-17
NO990363L (no) 1999-01-26
UA55420C2 (uk) 2003-04-15
BG103119A (bg) 1999-10-29
SI9720051A (sl) 1999-10-31
CA2261894C (en) 2005-03-22
AU4010597A (en) 1998-02-25
ATE209175T1 (de) 2001-12-15
PL188010B1 (pl) 2004-11-30
USRE39074E1 (en) 2006-04-18
ZA976793B (en) 1998-02-02
ES2167781T3 (es) 2002-05-16
EP0915821B1 (de) 2001-11-21
RS49592B (sr) 2007-06-04
CZ31699A3 (cs) 1999-07-14
MY120427A (en) 2005-10-31
NZ333950A (en) 2000-08-25
WO1998005619A1 (de) 1998-02-12
NO990363D0 (no) 1999-01-26
NO323890B1 (no) 2007-07-16
BR9710906B1 (pt) 2011-06-14
ID18000A (id) 1998-02-19
BR9710906A (pt) 1999-08-17
CN100360493C (zh) 2008-01-09
DE59706053D1 (de) 2002-02-21

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