Multi-reactor system and method for production of polyethylene and ethylene co-polymers
AssigneeChevron Phillips Chemical Company LP
InventorKenneth Alan Dooley
Life of this patent
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Abstract
Multi-reactor systems for the production of low-density polyethylene (LDPE) polymers and copolymers, wherein a first reactor product stream has a total mass flow of from about 10% to about 80% of the total mass flow of the second reactor product stream, methods of using the same, and processes of monitoring the same.
Claims40
A method for the production of a low-density polyethylene polymer in a multi-reactor system comprising:
- adding a first ethylene-containing feed stream to a first polymerization reactor;
- polymerizing the first ethylene-containing feed stream in the first polymerization reactor in the presence of a first initiator to create a first reactor product stream;
- transferring the first reactor product stream from the first polymerization reactor to a second polymerization reactor;
- adding a second ethylene-containing feed stream to the second polymerization reactor;
- polymerizing the first reactor product stream and the second ethylene-containing feed stream in the presence of a second initiator to produce a second reactor product stream comprising a low-density polyethylene polymer;
- wherein the first reactor product stream has a total mass flow that is about 10% to about 80% of the total mass flow of the second reactor product stream.
A multi-reactor system for the production of low-density polyethylene polymers comprising:
- a first polymerization reactor configured to receive a first ethylene-containing feed stream and further configured to polymerize said ethylene-containing feed stream in the presence of a first initiator to create a first reactor product stream;
- a second polymerization reactor configured to receive the first reactor product stream and a second ethylene-containing feed stream and further configured to polymerize said first reactor product stream and second ethylene-containing feed stream in the presence of a second initiator to create a second reactor product stream comprising low-density polyethylene polymers;
- wherein the first polymerization reactor and the second polymerization reactor are configured such that the first reactor product stream has a total mass flow of from about 10% to about 80% of the total mass flow of the second reactor product stream.
A process for monitoring the polymerization of ethylene or ethylene and comonomers in the presence of a free-radical polymerization initiator at pressures from about 10,000 psi to about 50,000 psi and at temperatures from about 320° F. to about 600° F. in a multi-reactor system, comprising the steps of:
- a) providing a multi-reactor system comprising a first polymerization reactor and a second polymerization reactor, wherein an inner volume of the first polymerization reactor is from about 30% to about 50% of an inner volume of the second polymerization reactor;
- b) measuring as process parameters the temperature profiles and the pressures of reaction mediums and the flow and temperature profiles of cooling mediums along each of the first and second polymerization reactors,
- c) monitoring the feeds of ethylene, free-radical polymerization initiator, chain-transfer agent, and, optionally, comonomer to each of the first and second polymerization reactors,
- d) calculating, based on process parameters and on a model for the polymerization process, concentrations for free-radical polymerization initiator, chain transfer agent, ethylene, and, optionally, comonomers at a sufficient number of positions along each the first polymerization reactor and the second polymerization reactor such that at least one calculation is carried out each 10 seconds for a volume unit flowing through the first polymerization reactor,
- e) calculating, based on the measured process parameters and the calculated concentrations, the cooling power, the generation of heat, and the concentration of radicals,
- f) calculating, based on the calculated data of the cooling power, of the generation of heat, and of the concentration of radicals, the probability of a thermal runaway of the reaction mixture at the positions along each of the first polymerization reactor and the second polymerization reactor which have the highest temperatures, and
- g) outputting an alarm signal or activating an interlock if the calculated value for the probability of a thermal runaway in either the first polymerization reactor or second polymerization reactor exceeds a predefined value.
Dependencies are inferred from the claim text.