Etherification process
A liquid phase process is described for oligomerization of C[sub 4] and C[sub 5] isoolefins or the etherification thereof with C[sub 1] to C[sub 6] alcohols wherein the reactants are contacted in a reactor with a fixed bed acid cation exchange resin catalyst at an LHSV of 5 to 20, pressure of 0 to 400 psig and temperature of 120 to 300 F wherein the improvement is the operation of the reactor at a pressure to maintain the reaction mixture at its boiling point whereby at least a portion but less than all of the reaction mixture is vaporized. By operating at the boiling point and allowing a portion of the reaction mixture to vaporize, the exothermic heat of reaction is dissipated by the formation of more boil up and the temperature in the reactor is controlled. 2 figs.
- DOE Contract Number:
- FC07-80CS40454
- Assignee:
- Chemical Research Licensing Co., Houston, TX (United States)
- Patent Number(s):
- US 4950803; A
- Application Number:
- PPN: US 7-058698
- OSTI ID:
- 7023573
- Resource Relation:
- Patent File Date: 1 Jun 1987
- Country of Publication:
- United States
- Language:
- English
Similar Records
Reactor for exothermic reactions
Method for conducting exothermic reactions
Related Subjects
ALCOHOLS
CHEMICAL REACTIONS
ALKENES
POLYMERIZATION
CHEMICAL REACTORS
PRESSURE CONTROL
TEMPERATURE CONTROL
ETHERS
SYNTHESIS
FUEL ADDITIVES
BOILING POINTS
EVAPORATION
REACTION HEAT
ADDITIVES
CONTROL
ENTHALPY
HYDROCARBONS
HYDROXY COMPOUNDS
ORGANIC COMPOUNDS
ORGANIC OXYGEN COMPOUNDS
PHASE TRANSFORMATIONS
PHYSICAL PROPERTIES
THERMODYNAMIC PROPERTIES
TRANSITION TEMPERATURE
100200* - Synthetic Fuels- Production- (1990-)