KR840004521A - Method for preparing a catalyst made of gamma alumina - Google Patents

Method for preparing a catalyst made of gamma alumina Download PDF

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Publication number
KR840004521A
KR840004521A KR1019830002174A KR830002174A KR840004521A KR 840004521 A KR840004521 A KR 840004521A KR 1019830002174 A KR1019830002174 A KR 1019830002174A KR 830002174 A KR830002174 A KR 830002174A KR 840004521 A KR840004521 A KR 840004521A
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KR
South Korea
Prior art keywords
moles
sio
catalyst
group
gamma alumina
Prior art date
Application number
KR1019830002174A
Other languages
Korean (ko)
Inventor
휘라니(외 2) 오르훼오
Original Assignee
칼로 시오니
스남프로게리 쏘시에떼 피 아찌오니
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.)
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Publication date
Application filed by 칼로 시오니, 스남프로게리 쏘시에떼 피 아찌오니 filed Critical 칼로 시오니
Publication of KR840004521A publication Critical patent/KR840004521A/en

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • 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
    • B01J21/04—Alumina
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • 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
    • B01J23/74—Iron group metals
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/02—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the alkali- or alkaline earth metals or beryllium
    • B01J23/04—Alkali metals
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/08—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of gallium, indium or thallium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/10—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of rare earths
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
    • C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
    • C07C5/23—Rearrangement of carbon-to-carbon unsaturated bonds
    • C07C5/25—Migration of carbon-to-carbon double bonds
    • C07C5/2506—Catalytic processes
    • C07C5/2512—Catalytic processes with metal oxides

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

내용 없음No content

Description

감마 알루미나로된 촉매 제조방법Method for preparing a catalyst made of gamma alumina

본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음As this is a public information case, the full text was not included.

Claims (6)

aAl2O3. b SiO2.c MexOy의 일반 화학식을 만족시킴을 특징으로하는 감마알루미나로 된 촉매 단, 위의 식에서 MexOy는 ⅡA족과/또는 Ⅷ족과/또는 ⅢE족과/또는 란탄족 금속 산화물 1가지 이상이고 a,b,c는 각각 Al2O3.Si02및 MexOy의 몰수이며 b와 c는 다음과 같은 관계를 가짐aAl 2 O 3 . b SiO 2 .c Me x O y of the general formula of gamma alumina catalyst, characterized by satisfying the stage, the above formula Me x O y is ⅡA group and / or Ⅷ group and / or ⅢE group and / or lanthanum At least one group metal oxide, a, b, and c are the moles of Al 2 O 3 .Si0 2 and Me x O y , respectively, and b and c have the following relationship: C≥m.b+BC≥m.b + B 위의 식에서, B는 0.01과 같거나 이보다 큰 수이고, b는 0.020-0.250사이의 수이며, (b+c)/a비는 0.01-9.0사이에 있고, m은 0.7-0.1사이의 수임.Where B is a number equal to or greater than 0.01, b is a number between 0.020-0.250, the (b + c) / a ratio is between 0.01-9.0, and m is a number between 0.7-0.1. 청구범위 제1항에 있어서 MexOy는 La2O3이고 La2O3의 몰수는 다음과 같이 0.020-0.250사이의 SiO2의 몰수와 관계를 가진 촉매The catalyst of claim 1 wherein Me x O y is La 2 O 3 and the number of moles of La 2 O 3 is related to the number of moles of SiO 2 between 0.020-0.250 as follows: La2O3몰수≥0.257×SiO2몰수 +0.014Number of moles of La 2 O 3 ≥ 0.257 x number of moles of SiO 2 +0.014 청구범위 제1항에 있어서 MexOy는 Fe2O3이고, Fe2O3의 몰수는 다음과 같이 0.020-0.250사이의 SiO2몰수와 관계를 가진 촉매The catalyst of claim 1 wherein Me x O y is Fe 2 O 3, and the number of moles of Fe 2 O 3 is related to the number of moles of SiO 2 between 0.020-0.250 as follows. Fe2O3몰수≥0.290×SiO2몰수+0.018Number of moles of Fe 2 O 3 ≥ 0.290 × number of moles of SiO 2 +0.018 청구범위 제1항에 있어서, MexOy는 CaO이고 CaO의 몰수는 다음과 같이 0.020-0.250사이의 SiO2의 몰수와 관계를 가진 촉매The catalyst of claim 1 wherein Me x O y is CaO and the number of moles of CaO is related to the number of moles of SiO 2 between 0.020-0.250 as follows: CaO몰수≥0.500×SiO2몰수+0.030Number of moles of CaO ≥ 0.500 x number of moles of SiO 2 +0.030 청구범위 제1항에 있어서, MexOy는 BaO이고 BaO의 몰수는 다음과 같이 0.020-0.250사이의 SiO2의 몰수와 관계를 가진 촉매The catalyst of claim 1 wherein Me x O y is BaO and the number of moles of BaO is related to the number of moles of SiO 2 between 0.020-0.250 as follows. BaO몰수≥0.500×SiO2몰수+0.020Number of moles of BaO ≥ 0.500 x number of moles of SiO 2 +0.020 실리카에 의해 안정화된 감마 알루미나를 ⅡA족과/또는 Ⅷ족과/또는 ⅢB족과/또는 란탄족의 금속임 수용액으로 함침시켜 청구범위 제1항의 조성물을 제조함을 특징으로 하는 실리카에 의해 안정화된 감마 아루미나로 된 촉매 제조방법.Gamma alumina stabilized by silica is impregnated with an aqueous solution of Group IIA and / or Group VIII and / or Group IIIB and / or Lanthanum, to prepare the composition of claim 1. Method for preparing a catalyst made of gamma alumina. ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.※ Note: The disclosure is based on the initial application.
KR1019830002174A 1982-05-27 1983-05-18 Method for preparing a catalyst made of gamma alumina KR840004521A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IT21512A/82 1982-05-27
IT21512/82A IT1152198B (en) 1982-05-27 1982-05-27 ALBUMINE RANGE CATALYST AND ITS PREPARATION METHOD

Publications (1)

Publication Number Publication Date
KR840004521A true KR840004521A (en) 1984-10-22

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ID=11182900

Family Applications (1)

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KR1019830002174A KR840004521A (en) 1982-05-27 1983-05-18 Method for preparing a catalyst made of gamma alumina

Country Status (29)

Country Link
JP (1) JPS58216741A (en)
KR (1) KR840004521A (en)
AU (1) AU557471B2 (en)
BE (1) BE896851A (en)
CA (1) CA1193238A (en)
CS (1) CS239938B2 (en)
DD (2) DD211720A5 (en)
DE (1) DE3319099A1 (en)
DK (1) DK234483A (en)
EG (1) EG16047A (en)
ES (1) ES8505833A1 (en)
FR (1) FR2527941A1 (en)
GB (1) GB2121698B (en)
GR (1) GR78565B (en)
HU (1) HU200709B (en)
IT (1) IT1152198B (en)
LU (1) LU84824A1 (en)
NL (1) NL8301873A (en)
NO (1) NO158485C (en)
NZ (1) NZ204199A (en)
PH (1) PH17970A (en)
PL (1) PL140654B1 (en)
PT (1) PT76765B (en)
RO (1) RO86664B (en)
SE (1) SE452954B (en)
SU (1) SU1440330A3 (en)
YU (1) YU44435B (en)
ZA (1) ZA833399B (en)
ZW (1) ZW11383A1 (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61157345A (en) * 1984-12-28 1986-07-17 Toyo C C I Kk Carrier for catalyst
DE3839580C1 (en) * 1988-11-24 1990-07-05 Condea Chemie Gmbh, 2212 Brunsbuettel, De
US5187138A (en) * 1991-09-16 1993-02-16 Exxon Research And Engineering Company Silica modified hydroisomerization catalyst
US5208200A (en) * 1992-02-27 1993-05-04 Exxon Research And Engineering Co. Noble metal on rare earth modified silica alumina as hydrocarbon conversion catalyst
US5248409A (en) * 1992-02-27 1993-09-28 Exxon Research & Engineering Company Metal on rare earth modified silica alumina as hydrocarbon conversion catalyst
DE4445680A1 (en) * 1994-12-21 1996-06-27 Huels Chemische Werke Ag Catalyst and process for the isomerization of aliphatic C¶4¶-C¶1¶¶¶ monoolefins
DE102013226370A1 (en) 2013-12-18 2015-06-18 Evonik Industries Ag Production of butadiene by oxidative dehydrogenation of n-butene after prior isomerization
DE102015200702A1 (en) 2015-01-19 2016-07-21 Evonik Degussa Gmbh Preparation of butadiene from ethene
JP6571392B2 (en) 2015-05-29 2019-09-04 Ｊｘｔｇエネルギー株式会社 Isomerization catalyst, linear olefin production method and compound production method
JP6736017B2 (en) * 2015-11-05 2020-08-05 Ｅｎｅｏｓ株式会社 Isomerization catalyst, method for producing linear olefin and method for producing compound

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2461069A (en) * 1944-06-10 1949-02-08 Socony Vacuum Oil Co Inc Simultaneous catalytic cracking and desulfurization of hydrocarbons
US3313858A (en) * 1965-02-12 1967-04-11 Phillips Petroleum Co Isomerization of non-terminal olefins
US3925253A (en) * 1973-03-19 1975-12-09 Ethyl Corp Catalysts
US4220559A (en) * 1978-02-14 1980-09-02 Engelhard Minerals & Chemicals Corporation High temperature-stable catalyst composition
FR2424061A1 (en) * 1978-04-25 1979-11-23 Lyon Applic Catalytiques NEW CONTACT MASS FOR HETEROGENOUS CATALYSIS
JPS6035174B2 (en) * 1979-05-10 1985-08-13 株式会社日本触媒 Catalyst for producing alkylene glycol ethers

Also Published As

Publication number Publication date
GB2121698A (en) 1984-01-04
CA1193238A (en) 1985-09-10
PH17970A (en) 1985-02-22
DD211720A5 (en) 1984-07-25
NL8301873A (en) 1983-12-16
PL242188A1 (en) 1984-07-02
SE8302769D0 (en) 1983-05-17
CS239938B2 (en) 1986-01-16
FR2527941A1 (en) 1983-12-09
AU1483583A (en) 1983-12-01
RO86664A (en) 1985-04-17
JPS58216741A (en) 1983-12-16
EG16047A (en) 1987-04-30
BE896851A (en) 1983-11-28
DK234483D0 (en) 1983-05-25
DE3319099A1 (en) 1983-12-01
SU1440330A3 (en) 1988-11-23
YU109983A (en) 1985-12-31
ES523075A0 (en) 1985-06-16
PT76765A (en) 1983-06-01
RO86664B (en) 1985-05-01
IT8221512A0 (en) 1982-05-27
GB8313562D0 (en) 1983-06-22
SE8302769L (en) 1983-11-28
ZA833399B (en) 1984-05-30
GB2121698B (en) 1986-04-23
SE452954B (en) 1988-01-04
AU557471B2 (en) 1986-12-24
ZW11383A1 (en) 1983-07-27
PT76765B (en) 1986-03-27
DD228538A5 (en) 1985-10-16
PL140654B1 (en) 1987-05-30
HU200709B (en) 1990-08-28
NO158485B (en) 1988-06-13
NZ204199A (en) 1985-11-08
IT1152198B (en) 1986-12-31
LU84824A1 (en) 1984-03-07
NO831848L (en) 1983-11-28
HUT34370A (en) 1985-03-28
DE3319099C2 (en) 1987-06-11
ES8505833A1 (en) 1985-06-16
DK234483A (en) 1983-11-28
GR78565B (en) 1984-09-27
NO158485C (en) 1988-09-21
YU44435B (en) 1990-08-31

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