Reaction configuration and procedure for polymers production

Patent metadata

Field	Value
Publication number	US-11834530-B2
Application number	US-201917252013-A
Country	US
Kind code	B2
Filing date	Jun 11, 2019
Priority date	Jun 14, 2018
Publication date	Dec 5, 2023
Grant date	Dec 5, 2023

Abstract

There is a procedure for polymerisation in solution for the production of polymers. The procedure has the following steps: (A) continuously feeding one or more monomers, one or more solvents in a quantity comprised between 70% and 90% by weight with respect to the reagent mixture, and a catalytic system, to a first stirred reaction volume, wherein a single mixing cell is formed, in which the polymerisation begins, until a conversion is attained that varies from 20% to 70% with respect to the final conversion achieved and (B) proceeding the polymerisation in at least one second stirred reaction volume connected in series to the first reaction volume, in which two or more mixing cells are formed, at the outlet of which the final conversion of the monomer is attained. In the first reaction volume, the average residence time of the reagent mixture varies within an interval ranging from 10% to 25% with respect to the average residence time of the entire reaction volume.

First claim

The invention claimed is:

1. A procedure of polymerisation in solution for the production of polymers, comprising the following steps:
continuously feeding one or more monomers, one or more solvents in a quantity comprised between 70% and 90% by weight, and a catalytic system, to a first stirred reaction volume, wherein a single mixing cell is formed, in which the polymerisation begins until a conversion is attained that varies from 20% to 70% with respect to the final conversion achieved,
proceeding the polymerisation in at least one second stirred reaction volume connected in series to the first reaction volume, in which two or more mixing cells are formed, at the outlet of which the final conversion of the monomer is attained;
wherein in the first reaction volume the average residence time of the reagent mixture varies within an interval ranging from 10% to 25% with respect to the average residence time of the entire reaction volume.

2. The procedure according to claim 1 , wherein, in the first reaction volume, the specific stirring power is greater than the specific stirring power of the volumes subsequent to the first.

3. The procedure according to claim 2 , wherein, in the first reaction volume, the specific stirring power is greater than 2 kW/m 3 .

4. The procedure according to claim 3 , wherein, in the reaction volumes subsequent to the first volume the specific stirring power is comprised between 1 kW/m 3 and 2 kW/m 3 .

5. The procedure according to claim 1 , wherein the average residence time of the entire reaction volume is between 1 hour and 2 hours.

6. The polymerisation procedure for the production of polymers according to claim 1 , wherein the average residence time of the one or more monomers in the first reaction volume varies from 15% to 20% of the total residence time of the entire reaction volume.

7. The polymerisation procedure for the production of polymers according to claim 1 , wherein the one or more monomers is selected from butadiene, styrene, isoprene, acrylonitrile, olefins or diolefins, and mixtures thereof.

8. The polymerisation procedure for the production of polymers according to claim 7 , wherein the monomer is 1,3-butadiene.

9. The polymerisation procedure for the production of polymers according to claim 1 , wherein the one or more solvents is selected from hexanes, pentanes, heptanes, and mixtures thereof.

10. A reaction configuration for the production of a polymer comprising: a first stirred reactor and one or more second stirred reactors subsequent to the first stirred tank connected in series,
wherein the first stirred reactor is a single mixing cell and has a reaction volume equal to a value varying from 1/10 to ¼ with respect to the total reaction volume, wherein the total reaction volume is the sum of the reaction volumes of all reactors present;
wherein the reactors subsequent to the first, connected in series, each have a reaction volume in which two or more mixing cells are present.

11. The reaction configuration according to claim 10 , wherein the reaction volume of the first reactor varies from ⅛ to ⅕ of the total reaction volume, wherein the total reaction volume is the sum of the reaction volumes of all reactors present.

12. The reaction configuration according to claim 11 , wherein the number of reactors ranges from 2 to 5.

13. The reaction configuration according to claim 10 , wherein the first reactor is equipped with agitator stirring device having a single Rushton radial flow impeller, or two or more Hydrofoil axial flow impellers.

14. The reaction configuration according to claim 10 , wherein the reactors subsequent to the first are equipped with an agitator device having two or more Rushton radial flow impellers.

Assignees

• Versalis Spa

Inventors

• Marchetti Gianni
• Regattieri Giovanni

Classifications

• C08F2/01 Primary

  characterised by special features of the polymerisation apparatus used · CPC title

• C08F2/06 Primary

  Organic solvent · CPC title

• C08F36/06 Primary

  Butadiene · CPC title

• C08F10/00

  Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond · CPC title