GB1011270A - Selective hydrogenation procedure and catalyst therefor - Google Patents
Selective hydrogenation procedure and catalyst thereforInfo
- Publication number
- GB1011270A GB1011270A GB10847/63A GB1084763A GB1011270A GB 1011270 A GB1011270 A GB 1011270A GB 10847/63 A GB10847/63 A GB 10847/63A GB 1084763 A GB1084763 A GB 1084763A GB 1011270 A GB1011270 A GB 1011270A
- Authority
- GB
- United Kingdom
- Prior art keywords
- surface pores
- hydrocarbons
- acetylenic
- hydrogen
- gas
- Prior art date
- Legal status (The legal status 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 status listed.)
- Expired
Links
Classifications
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- 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
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/54—Catalysts 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
- B01J23/56—Platinum group metals
- B01J23/64—Platinum group metals with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/652—Chromium, molybdenum or tungsten
- B01J23/6522—Chromium
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- 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
- C07C5/02—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation
- C07C5/03—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation of non-aromatic carbon-to-carbon double bonds
-
- 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
- C07C5/02—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation
- C07C5/08—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation of carbon-to-carbon triple bonds
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- C07C2523/24—Chromium, molybdenum or tungsten
- C07C2523/26—Chromium
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
- C07C2523/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals of the platinum group metals
- C07C2523/44—Palladium
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
- C07C2523/54—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals combined with metals, oxides or hydroxides provided for in groups C07C2523/02 - C07C2523/36
- C07C2523/56—Platinum group metals
- C07C2523/64—Platinum group metals with arsenic, antimony, bismuth, vanadium, niobium, tatalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- C07C2523/652—Chromium, molybdenum or tungsten
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
Abstract
A method of selectively hydrogenating acetylenic and/or diolefinic hydrocarbons in a gas wherein the major proportion of the unsaturated hydrocarbons is olefinic, comprises contacting the gas, admixed with a quantity of hydrogen sufficient to reduce the acetylenic and/or diolefinic hydrocarbons to olefines, with a Pd and Cr on Al2O3 catalyst such that the Al2O3 has a pore volume of surface pores of between 0 and 0.4 c.c./gm., the surface pores having a threshold diameter not exceeding 800 <\>rA, the weight ratio of Pd to Cr being in the range 2 : 1 to 2 : 3. Comparative examples are given in which gas streams contain propadiene, methyl acetylene, propylene, propane, hydrogen and methane are selectively hydrogenated and the hydrogenation of vinyl acetylene to 1 : 3 butadiene in the presence of 1 : 3 butadiene is described. Reaction is effected at 100-400 DEG F., 50-500 p.s.i.g., and a G.H.S.V. of 50-2000 with an amount of hydrogen 1.2-4 times the stoichiometric amount.ALSO:Acetylenic hydrocarbons in an olefin stream are selectively hydrogenated in the presence of a catalyst comprising 0,01-0,5% Pd metal and 0,01-0,5% Cr metal on an alumina carrier having a pore volume of surface pores of between 0 and 0,4 c.c./gm., the surface pores having a threshold diameter not exceeding 800 and such that the weight ratio of Pd to Cr is in the range from 2:1 to 1:1,5. Comparative examples are given.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB10847/63A GB1011270A (en) | 1963-03-19 | 1963-03-19 | Selective hydrogenation procedure and catalyst therefor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB10847/63A GB1011270A (en) | 1963-03-19 | 1963-03-19 | Selective hydrogenation procedure and catalyst therefor |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1011270A true GB1011270A (en) | 1965-11-24 |
Family
ID=9975416
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB10847/63A Expired GB1011270A (en) | 1963-03-19 | 1963-03-19 | Selective hydrogenation procedure and catalyst therefor |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB1011270A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0087980A1 (en) * | 1982-03-02 | 1983-09-07 | Sumitomo Chemical Company, Limited | Method of selective hydrogenation of hydrocarbons |
US7335800B2 (en) | 2005-04-21 | 2008-02-26 | Shell Oil Company | Hydrogenation catalyst and hydrogenation method |
US7381852B2 (en) | 2006-04-13 | 2008-06-03 | Shell Oil Company | Process for hydrogenating an aldehyde |
US7777085B2 (en) | 2008-10-01 | 2010-08-17 | Inventure Chemical, Inc. | Method for conversion of oil-containing algae to 1,3-propanediol |
US7943792B2 (en) | 2007-04-02 | 2011-05-17 | Inventure Chemical Inc. | Production of biodiesel, cellulosic sugars, and peptides from the simultaneous esterification and alcoholysis/hydrolysis of materials with oil-containing substituents including phospholipids and peptidic content |
US8212062B2 (en) | 2007-04-02 | 2012-07-03 | Inventure Chemical, Inc. | Production of biodiesel, cellulosic sugars, and peptides from the simultaneous esterification and alcoholysis/hydrolysis of oil-containing materials with cellulosic and peptidic content |
-
1963
- 1963-03-19 GB GB10847/63A patent/GB1011270A/en not_active Expired
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0087980A1 (en) * | 1982-03-02 | 1983-09-07 | Sumitomo Chemical Company, Limited | Method of selective hydrogenation of hydrocarbons |
US7335800B2 (en) | 2005-04-21 | 2008-02-26 | Shell Oil Company | Hydrogenation catalyst and hydrogenation method |
US7381852B2 (en) | 2006-04-13 | 2008-06-03 | Shell Oil Company | Process for hydrogenating an aldehyde |
US7943792B2 (en) | 2007-04-02 | 2011-05-17 | Inventure Chemical Inc. | Production of biodiesel, cellulosic sugars, and peptides from the simultaneous esterification and alcoholysis/hydrolysis of materials with oil-containing substituents including phospholipids and peptidic content |
US8212062B2 (en) | 2007-04-02 | 2012-07-03 | Inventure Chemical, Inc. | Production of biodiesel, cellulosic sugars, and peptides from the simultaneous esterification and alcoholysis/hydrolysis of oil-containing materials with cellulosic and peptidic content |
US8592613B2 (en) | 2007-04-02 | 2013-11-26 | Inventure Renewables, Inc. | Production of biodiesel, cellulosic sugars, and peptides from the simultaneous esterification and alcoholysis/hydrolysis of materials with oil-containing substituents including phospholipids and cellulosic and peptidic content |
US7777085B2 (en) | 2008-10-01 | 2010-08-17 | Inventure Chemical, Inc. | Method for conversion of oil-containing algae to 1,3-propanediol |
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