GB677480A - Polymerization of normally gaseous olefines - Google Patents
Polymerization of normally gaseous olefinesInfo
- Publication number
- GB677480A GB677480A GB13881/50A GB1388150A GB677480A GB 677480 A GB677480 A GB 677480A GB 13881/50 A GB13881/50 A GB 13881/50A GB 1388150 A GB1388150 A GB 1388150A GB 677480 A GB677480 A GB 677480A
- Authority
- GB
- United Kingdom
- Prior art keywords
- acid
- mol
- concentration
- phosphoric acid
- per cent
- 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
-
- 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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/02—Apparatus characterised by being constructed of material selected for its chemically-resistant properties
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/02—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons
- C07C2/04—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation
- C07C2/06—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation of alkenes, i.e. acyclic hydrocarbons having only one carbon-to-carbon double bond
- C07C2/08—Catalytic processes
- C07C2/14—Catalytic processes with inorganic acids; with salts or anhydrides of acids
- C07C2/18—Acids of phosphorus; Salts thereof; Phosphorus oxides
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/02—Apparatus characterised by their chemically-resistant properties
- B01J2219/0204—Apparatus characterised by their chemically-resistant properties comprising coatings on the surfaces in direct contact with the reactive components
- B01J2219/0236—Metal based
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2527/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- C07C2527/14—Phosphorus; Compounds thereof
- C07C2527/16—Phosphorus; Compounds thereof containing oxygen
- C07C2527/167—Phosphates or other compounds comprising the anion (PnO3n+1)(n+2)-
- C07C2527/173—Phosphoric acid or other acids with the formula Hn+2PnO3n+1
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
In polymerizing normally gaseous olefins with concentrated liquid phosphoric acid in a polymerization zone presenting acid-resistant metallic surfaces, corrosion thereof is decreased by maintaining the concentration of phosphoric acid esters of olefins in the reaction mixture below 0.08 mol. per mol. of free phosphoric acid. Ethylene, propylene, and butylenes may be polymerized with phosphoric acid of above about 90 per cent, calculated as ortho acid, at 150-450 DEG F., above 100 p.s.i.g., and space velocities above 0.5 vol. liquid olefin/vol. catalyst/hour. Ester concentration gradually increases to an equilibrium value. The mixture of acid and hydrocarbons leaving the reactor is stratified, the hydrocarbon being neutralized and utilized for motor fuel while the acid layer is recycled after part thereof is heated to about 500 DEG F., if desired at atmospheric or lower pressure, to decompose contained esters. Ester concentration may also be controlled by reducing the olefin feed rate which is ordinarily 0.5-20 v./v./hour, to a figure within this range to bring the concentration below 0.08 mol./mol. acid. Alternatively, or additionally, temperature may be raised to decrease the ester concentration. The relation between ester concentration and corrosion rates of silver and a high nickel, molybdenum, iron alloy is illustrated using an initial acid of 103 per cent, calculated as orthophosphoric, and temperature of 300 DEG F., with a feed containing 28-45 per cent propylene. Corrosion rates of high chrome-nickel austenitic alloys and copper are also given.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US677480XA | 1949-06-04 | 1949-06-04 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB677480A true GB677480A (en) | 1952-08-13 |
Family
ID=22078132
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB13881/50A Expired GB677480A (en) | 1949-06-04 | 1950-06-02 | Polymerization of normally gaseous olefines |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB677480A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0237175A1 (en) * | 1986-02-05 | 1987-09-16 | Exxon Chemical Patents Inc. | Improved process for reducing fouling in higher olefin plants |
WO2002049754A1 (en) * | 2000-12-21 | 2002-06-27 | Solarworld Aktiengesellschaft | Fluidised bed reactor made of a nickel-chrome-molybdenum-alloy for the synthesis of trichlorosilane |
-
1950
- 1950-06-02 GB GB13881/50A patent/GB677480A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0237175A1 (en) * | 1986-02-05 | 1987-09-16 | Exxon Chemical Patents Inc. | Improved process for reducing fouling in higher olefin plants |
WO2002049754A1 (en) * | 2000-12-21 | 2002-06-27 | Solarworld Aktiengesellschaft | Fluidised bed reactor made of a nickel-chrome-molybdenum-alloy for the synthesis of trichlorosilane |
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