Polymer property distribution functions methodology and simulators

• US 6,093,211 A
• Filed: 04/09/1998
• Issued: 07/25/2000
• Est. Priority Date: 04/09/1998
• Status: Expired due to Term

• Current Assignee: Aspentech Corporation
• Original Assignee: Aspen Technology Inc (Emerson Electric Company)
• Inventors: Sirohi, Ashuraj, Hamielec, Alvin E., Osias, Martine, Chen, Chau-Chyun, Ramanathan, Sundaram
• Primary Examiner(s): Teska, Kevin J.
• Assistant Examiner(s): Sergent, Douglas W.
• Application Number:
  US09/057,795
• Time in Patent Office: 838 Days
• Field of Search: 395/500.33, 395/500.27, 395/500.23, 702/31, 702/30, 364/528.01, 364/528.08, 526/79
• US Class Current: 703/12
• CPC Class Codes: B01J 19/0006 Controlling or regulating processes controlling or regulating in general G05
• CPC Class Codes: C08F 10/00 Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
• CPC Class Codes: C08F 2/00 Processes of polymerisation
• CPC Class Codes: C08F 2400/02 Control or adjustment of polymerization parameters
• CPC Class Codes: G05B 17/02 electric

Abstract

A process simulator and modeling methodology employs instantaneous property measures. The instantaneous measures of various polymer properties are tracked throughout the subject polymer manufacturing system and used to calculate respective property distribution functions. For example, property distributions of composition, molecular weight, stereoregularity and long chain branching are calculated, tracked in time and location throughout the manufacturing system, and used to model the polymer manufacturing system and polymerization process performed by the system. More specifically, the present invention calculates full distribution of polymer properties from the instantaneous property measures and tracked instantaneous property distributions. This enables accurate and computationally efficient modeling of the polymerization process and manufacturing system for carrying out the same. The present invention method and apparatus thus enables modeling of polymer manufacturing systems (a) operating under transient or steady-state conditions, using free radicals or catalysts with a plurality of active center types, and having reactor types of CSTR, PFTR or any combinations thereof operating in batch, semi-batch or continuous operation, and (b) for carrying out polymerization processes including solution, slurry, gas phase, suspension and emulsion polymerizations.

Claims

1. In a digital processor, a method for modeling a polymerization process carried out in a polymer manufacturing system formed of plural reactors and ancillary equipment, the method comprising the steps of:

receiving indications of reactor type and polymers involved in the polymerization process, each polymer having at least one molecular property;

determining instantaneous property measures of the molecular properties of the polymers;

generating and tracking respective instantaneous property distributions of the molecular properties from the determined instantaneous property measures;

from the instantaneous property distributions, calculating full distributions of the molecular properties at any location in the manufacturing system;

using the calculated full property distributions, forming and reporting a model of the polymerization process such that the polymer manufacturing system is modeled; and

the method being capable of modeling both linear and non-linear polymerization processes.

2. A method as claimed in claim 1 wherein the step of determining instantaneous property measures includes calculating and tracking instantaneous property measures of the molecular properties throughout the polymer manufacturing system.

3. A method as claimed in claim 1 wherein the molecular properties include molecular weight, composition, stereoregularity and long chain branching, and

the step of determining instantaneous property measures includes calculating at least one of molecular weight, composition, stereoregularity and long chain branching.

4. A method as claimed in claim 1 wherein the step of generating and tracking instantaneous distributions includes determining instantaneous property distribution functions of the molecular properties.

5. A method as claimed in claim 1 wherein the step of receiving indications includes an end-user specifying reactor type of batch, semi-batch or continuous operation.

6. A method as claimed in claim 5 wherein the step of end-user specifying includes specifying multiple continuous reactors in steady state.

7. A method as claimed in claim 5 wherein the step of end-user specifying includes specifying multiple transient continuous reactors.

8. A method as claimed in claim 1 wherein the step of generating and tracking includes calculating and tracking respective mass of pulses of polymers produced in the reactors of the polymer manufacturing system.

9. A computer based simulator for simulating a polymer manufacturing system formed of plural reactors and ancillary equipment for carrying out a polymerization process, the simulator comprising:

input means supportable by a digital processor, for enabling an end-user to provide indications of reactor type and polymers involved in the polymerization process, each polymer having at least one molecular property;

a calculating member responsive to the input means for determining instantaneous property measures of the molecular properties of the polymers throughout the polymer manufacturing system, and from the determined instantaneous property measure, the calculating member calculating full property distributions at any location in the manufacturing system, said full property distributions at any location in the manufacturing system forming a model of the polymerization process;

a reporter coupled to the calculating member for reporting the model of the polymerization process using the calculated full property distributions, such that the polymer manufacturing system is modeled; and

the simulator being capable of simulating both linear and non-linear polymerization processes.

10. A simulator as claimed in claim 9 further comprising a tracking member coupled to the calculating member, the tracking member tracking instantaneous property measures and instantaneous distributions of the properties, including respective mass of pulses of polymers produced in the reactors of the polymer manufacturing system, throughout the polymer manufacturing system.

11. A simulator as claimed in claim 9 wherein the molecular properties include molecular weight, composition, stereoregularity and long chain branching, and

the calculating member determines at least one of instantaneous molecular weight measures, instantaneous composition measures, stereoregularity and instantaneous long chain branching measures.

12. A simulator as claimed in claim 9 wherein the calculating member further determines property distribution functions of the molecular properties.

13. A simulator as claimed in claim 9 wherein the input means further enables an end-user to specify reactor type of batch, semi-batch or continuous operation.

14. A simulator as claimed in claim 13 wherein the end-user specifying includes specifying multiple continuous reactors in steady state.

15. A simulator as claimed in claim 13 wherein the end-user specifying includes specifying multiple transient continuous reactors.

16. A method of tracking polymer properties, including molecular, rheological and mechanical properties, of pulses of polymer produced in a polymerization process of a polymer manufacturing system, there being a plurality of site types produced in the polymerization process, and the manufacturing system including polymer reactors and ancillary equipment, comprising the steps of:

(i) identifying a mass and birth time of polymer pulses formed on each one of plural reactors and ancillary equipment in the polymer manufacturing system;

(ii) for each polymer pulse, obtaining instantaneous property measures of the polymer properties at birth time of the pulse and thereafter in the polymer manufacturing system; and

(iii) summing the obtained instantaneous property measures of the polymer pulses across all pulses formed in the polymer manufacturing system, to determine full distributions of the polymer properties for a composite polymer at any point in the manufacturing system, the method being capable of tracking both linear and non-linear polymerization processes.

17. A method as claimed in claim 16 wherein the step of obtaining includes calculating the instantaneous property measures of polymer properties including at least one of molecular properties, rheological properties and mechanical properties.

18. A method as claimed in claim 16 wherein the step of obtaining further includes calculating the instantaneous properties of the polymer pulses at various times and points in the polymer manufacturing system.

19. A method as claimed in claim 16 wherein the method further includes the step of using computer means to perform the steps of (i), (ii) and (iii).

20. A method as claimed in claim 19 wherein the method further includes the step of modeling the polymer manufacturing system from the determined full distributions of the polymer properties.

21. A method as claimed in claim 16 wherein

the polymer manufacturing system is operating under transient or steady-state conditions using catalysts or free radicals with a plurality of active center types;

the polymerization process includes at least one of solution, slurry, gas phase, suspension and emulsion polymerization, and

the polymer reactors (a) have a respective operator type of one of batch, semi-batch and continuous operation, and (b) include one of a continuous stirred tank reactor, a plug flow tank reactor and any combination thereof; and

the method further includes the step of modeling the polymer manufacturing system from the determined full distributions of the polymer properties.

22. A method as claimed in claim 21 wherein the method further includes the step of employing computer means to perform the steps of (i), (ii) and (iii).

23. A method as claimed in claim 16 wherein the step of summing includes employing appropriate mixing rules to determine respective full distributions of polymer properties of the composite polymer, said polymer properties including at least one of molecular properties, rheological properties and mechanical properties.