Device and methods to actively control the production of multi-stage polymer production
Devices and methods for actively controlling the production of multistage and multimodal polymers. The device may include a reaction vessel configured to contain a polymer solution and generate polymer reactions in at least two stages as well as one or more detectors configured to monitor at least one reaction characteristic of the polymer solution contained in the reaction vessel. The device may further include a controller coupled with the reaction vessel and the one or more detectors, the controller configured to actively control the development of a predetermined reaction characteristic by modifying at least one process control variable based on the at least one reaction characteristic monitored by the detector.
1 . A method for producing multimodal polymers in a reaction vessel that is configured to contain a polymer solution that undergoes polymer reactions in at least two stages to produce multimodal polymers comprising a first mode and a second mode, the method comprising:
generating polymer reactions in at least two stages in the reaction vessel;
monitoring at least one reaction characteristic in at least one stage;
determining a reaction trajectory based on the at least one monitored reaction characteristic:
actively controlling development of the first mode by modifying at least one process control variable based on the at least one monitored reaction characteristic during production of the polymer in at least one of the at least two stages, wherein the at least one process control variable is modified based on the reaction trajectory to follow a first target trajectory;
determining a second target trajectory associated with development of the second mode;
and actively controlling the development of the second mode by modifying at least one process control variable based on the reaction trajectory to follow the second target trajectory.
2 . The method according to claim 1 , wherein the at least one reaction characteristic is molecular weight.
3 . The method according to claim 1 , wherein the at least one reaction characteristic is copolymer composition.
4 . The method according to claim 1 , wherein the at least one reaction characteristic is intrinsic viscosity (IV).
5 . The method according to claim 1 , further comprising:
determining a plurality of reaction trajectories simultaneously, each of the plurality of reaction trajectories based on at least one monitored reaction characteristic; and
modifying one or more process control variables based on the plurality of reaction trajectories, such that the trajectory of a plurality of monitored reaction characteristics are controlled simultaneously; wherein the plurality of simultaneously controlled trajectories are selected from the group consisting of reduced viscosity, IV, conversion, monomer and polymer concentrations, comonomer composition, branching, degree of hydrolysis, and chemical substitution.
6 . The method according to claim 1 , wherein the at least one characteristic of the first mode or the second mode is selected from the group consisting of Mw, reduced viscosity, conversion, monomer and polymer concentrations, comonomer composition, branching, degree of hydrolysis, and chemical substitution.
7 . The method according to claim 1 , wherein the process control variable is selected from the group consisting of temperature, stirring rate, mixing rate, agitation, introduction of monomers, introduction of comonomers, introduction of an initiator, introduction of a quencher, introduction of a branching agent, introduction of a cross-linking agent, introduction of a chain transfer agent, introduction of an inhibitor, introduction of air, introduction of O 2 gas, introduction of N 2 gas, introduction of argon gas, introduction of an acid, introduction of a base, introduction of a redox agent, and introduction of a catalyst.
8 . A device comprising:
a reaction vessel configured to contain a polymer solution to undergo polymer reactions in at least two stages to produce multi-modal polymers comprising a first mode and a second mode, wherein the at least two stages yield polymers in the respective stages with distinct characteristics;
one or more detectors configured to monitor at least one reaction characteristic of the polymer solution contained in the reaction vessel; and
a controller coupled with the reaction vessel and the one or more detectors, the controller is configured to determine a reaction trajectory based on the at least one monitored reaction characteristic and to actively control development of the the first mode by modifying at least one process control variable based on the at least one reaction characteristic monitored by the detector during production of the polymer in at least one of the at least two stages,
wherein the at least one process control variable is modified based on the reaction trajectory to follow a first target trajectory;
wherein the controller is further configured to determine a second target trajectory associated with the development of the second mode, and to actively control development of the second mode by modifying the at least one process control variable based on the at least one reaction characteristic monitored by the detector to follow the second target trajectory.
9 . The device according to claim 8 , wherein the controller further comprises an interface configured to allow an operator to cause the controller to control the development of a predetermined reaction characteristic.
10 . The device according to claim 8 , wherein the controller is further configured to:
determine a plurality of reaction trajectories simultaneously, each of the plurality of reaction trajectories based on at least one monitored reaction characteristic; and
modify one or more process control variables based on the plurality of reaction trajectories, such that the trajectory of a plurality of monitored reaction characteristics are controlled simultaneously;
wherein the plurality of simultaneously controlled trajectories are selected from the group consisting of reduced viscosity, IV, conversion, monomer and polymer concentrations, comonomer composition, branching, degree of hydrolysis, and chemical substitution.
11 . The device according to claim 8 , wherein the detector and controller are components of an ACOMP system.
12 . The device according to claim 8 , wherein the at least one process control variable is modified based on difference between the reaction trajectory and the second target trajectory.
13 . The device according to claim 8 , wherein the reaction vessel comprises a plurality of continuously stirred tank reactors (CSTRs) placed in serial flow to reach different stages in controlled multi-stage process.
14 . The device according to claim 8 , wherein the reaction vessel comprises a first reactor for a first stage of reaction and a second reactor for a second stage of reaction.