FR2314164A1 - Propylene disproportionation to ethylene and 2-butene - with molybdenum oxide alumina catalyst in liq. phase using hydrocarbon solvent - Google Patents
Propylene disproportionation to ethylene and 2-butene - with molybdenum oxide alumina catalyst in liq. phase using hydrocarbon solventInfo
- Publication number
- FR2314164A1 FR2314164A1 FR7517970A FR7517970A FR2314164A1 FR 2314164 A1 FR2314164 A1 FR 2314164A1 FR 7517970 A FR7517970 A FR 7517970A FR 7517970 A FR7517970 A FR 7517970A FR 2314164 A1 FR2314164 A1 FR 2314164A1
- Authority
- FR
- France
- Prior art keywords
- butene
- ethylene
- liq
- phase
- catalyst
- 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.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C6/00—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions
- C07C6/02—Metathesis reactions at an unsaturated carbon-to-carbon bond
- C07C6/04—Metathesis reactions at an unsaturated carbon-to-carbon bond at a carbon-to-carbon double bond
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Propylene disproportionation, to ethylene and 2-butene, takes place in liq. phase with a Mo oxide-Al2O3 catalyst, at -40 to 100 degrees C, under standard press. to 200 kg/cm2. Novelty is carrying out process in a solvent consisting of paraffin, cycloparaffin, and/or aromatic hydrocarbons. Solvent : propylene vol. ratio is pref. 0.5 : 1 to 10 : 1. Side-reactions, e.g. polymerisation or isomerisation of 2-butene and catalyst deactivation by polymers, are prevented. Solvents easily dissolve any polymers and oligomers formed and remove them from catalyst surface. Process can be carried out for a long time at 100 degrees C and yields ethylene and 2-butene at constant rates. Solvents can be recoverd and re-used. Reaction velocity, catalyst activity and selectivity are improved. E.g. use of n-heptane in vol. ratio solvent/ C3H6 = 4 at LHSV 50, 80 degrees C, 50 atmos., improved max. C3H6 conversion from 25- to 46%, selectivity to ethylene and butene from 95- to 99% and ratio butene/ethylene from 1.65 to 0.995.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR7517970A FR2314164A1 (en) | 1975-06-09 | 1975-06-09 | Propylene disproportionation to ethylene and 2-butene - with molybdenum oxide alumina catalyst in liq. phase using hydrocarbon solvent |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR7517970A FR2314164A1 (en) | 1975-06-09 | 1975-06-09 | Propylene disproportionation to ethylene and 2-butene - with molybdenum oxide alumina catalyst in liq. phase using hydrocarbon solvent |
Publications (2)
Publication Number | Publication Date |
---|---|
FR2314164A1 true FR2314164A1 (en) | 1977-01-07 |
FR2314164B1 FR2314164B1 (en) | 1980-04-25 |
Family
ID=9156222
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
FR7517970A Granted FR2314164A1 (en) | 1975-06-09 | 1975-06-09 | Propylene disproportionation to ethylene and 2-butene - with molybdenum oxide alumina catalyst in liq. phase using hydrocarbon solvent |
Country Status (1)
Country | Link |
---|---|
FR (1) | FR2314164A1 (en) |
-
1975
- 1975-06-09 FR FR7517970A patent/FR2314164A1/en active Granted
Also Published As
Publication number | Publication date |
---|---|
FR2314164B1 (en) | 1980-04-25 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
ST | Notification of lapse |