IP Library › Granted Patent US 9,758,627
Granted Patent B2
US 9,758,627 · App. 14/909,936 · Granted Sep 12, 2017

Continuous manufacturing process for rubber masterbatch and rubber masterbatch prepared therefrom

Inventors: Mengjiao Wang (Bedford, MA); Jianjun Song (Shandong, CN); Deying Dai (Shandong, CN)
Assignee: EVE RUBBER INSTITUTE CO., LTD.
C08J3/226B29B7/30B29B7/58B29B7/7495B29B7/90C08K3/04C08K3/22C08L9/00C08J2309/00C08K2003/2296
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Quick Facts
Patent No.
US 9,758,627
App. No.
14/909,936
Granted
Sep 12, 2017
Kind
B2
Abstract

Disclosed are a continuous manufacturing process for a rubber masterbatch and a rubber masterbatch prepared therefrom. The manufacturing process comprises: 1): a filler is added to a rubber solution, forming a rubber/filler/solvent mixture by stirring; 2): the rubber/filler/solvent mixture obtained in step 1) is fed into a coagulator, and is coagulated after optionally being brought into contact and mixed with one or more fluids of nitrogen, steam, water, aqueous slurry of filler, and oil in the coagulator, resulting in a mixture of a rubber/filler composite and a solvent; 3): the mixture obtained in step 2) is directly passed into a heating medium at a temperature higher than the boiling point of the solvent, the polarity of the medium being different from that of the solvent used, the mixture is coagulated and deswelled, and the solvent is evaporated rapidly, thereby forming a mixture of a rubber/filler composite and the solvent containing the heating medium; and 4): the solvent is removed and the remaining mixture is dried, resulting in a rubber/filler masterbatch.

Claims (27)

1. A method for continuously producing a rubber masterbatch comprising:

1) adding a filler in a rubber solution, and stirring to form a rubber/filler/solvent mixture;

2) adding the rubber/filler/solvent mixture of step 1) into a coagulator, and optionally contacting and mixing with one or more fluid selected from the group consisting of nitrogen gas, water vapor, water, slurry of filler and oil so as to coagulate, resulting in a mixture of rubber/filler composite and the solvent;

3) adding the mixture obtained in step 2) directly into a heating medium with a temperature higher than the boiling point of the solvent, in which the polarity of the heating medium is different from that of the solvent, the mixture being further coagulated and deswollen, and the solvent being evaporated quickly so as to form a mixture of rubber/filler composite containing the heating medium as well as the solvent;

4) removing the solvent and drying the remaining mixture to obtain a rubber/filler masterbatch;

wherein step 3) is implemented in a tank container;

wherein the heating medium in step 3) is water, the solvent is a hydrocarbon solvent having a boiling point lower than 100° C., and optionally by vacuum drying, heat drying or extrusion heat drying for removal of water, the rubber/filler masterbatch is obtained;

wherein, the solvent evaporated in step 4) and the monomers not reacted in the synthesis of rubber access into a condenser and a fractionator for recycling, the heating medium is separated, and the mixture separated from the heating medium is transferred into a heating conveyer-belt type dryer and dried in vacuum, inert gas or air; alternatively, the solvent evaporated in step 4) and the monomers not reacted in the synthesis of rubber access into a condenser and a fractionator for recycling, and then, the remaining mixture is processed by extrusion heat drying.

2. The method according to claim 1 , wherein the solvent as removed in step 4) is recovered for recycling.

3. The method according to claim 1 , wherein one or more additives selected from oil, an anti-aging agent, a coupling agent, an active agent, an antioxidant, a flame retardant, a heat stabilizer, a light stabilizer, a dye, a pigment, a vulcanizing agent and an accelerating agent are added in step 1) and/or step 2).

4. The method according to claim 1 , wherein step 3) is implemented by using any container.

5. The method according to claim 1 , wherein said heat drying is oven drying or air drying.

6. The method according to claim 1 , wherein the extrusion heat drying comprises firstly extrusion to remove the heating medium, and then a further drying.

7. The method according to claim 6 , wherein said further drying is air drying, oven drying, or mechanical drying.

8. The method according to claim 7 , wherein said mechanical drying is performed using an open mill, kneading machine, internal mixer, continuous internal mixer, single-screw extruder, or twin-screw extruder.

9. A rubber masterbatch prepared by a method comprising:

1) adding a filler in a rubber solution, and stirring to form a rubber/filler/solvent mixture;

2) adding the rubber/filler/solvent mixture of step 1) into a coagulator, and optionally contacting and mixing with one or more fluid selected from the group consisting of nitrogen gas, water vapor, water, slurry of filler and oil so as to coagulate, resulting in a mixture of rubber/filler composite and the solvent;

3) adding the mixture obtained in step 2) directly into a heating medium with a temperature higher than the boiling point of the solvent, in which the polarity of the heating medium is different from that of the solvent, the mixture being further coagulated and deswollen, and the solvent being evaporated quickly so as to form a mixture of rubber/filler composite containing the heating medium as well as the solvent;

4) removing the solvent and drying the remaining mixture to obtain a rubber/filler masterbatch;

wherein step 3) is implemented in a tank container;

wherein the heating medium in step 3) is water, the solvent is a hydrocarbon solvent having a boiling point lower than 100° C., and optionally by vacuum drying, heat drying or extrusion heat drying for removal of water, the rubber/filler masterbatch is obtained;

wherein, the solvent evaporated in step 4) and the monomers not reacted in the synthesis of rubber access into a condenser and a fractionator for recycling, the heating medium is separated, and the mixture separated from the heating medium is transferred into a heating conveyer-belt type dryer and dried in vacuum, inert gas or air; alternatively, the solvent evaporated in step 4) and the monomers not reacted in the synthesis of rubber access into a condenser and a fractionator for recycling, and then, the remaining mixture is processed by extrusion heat drying.

10. A rubber article prepared by using the rubber masterbatch according to claim 9 .

11. The method according to claim 1 , wherein the tank container is a cylindrical tank container.

12. The method according to claim 1 , further comprising using the rubber masterbatch to prepare a rubber article.

13. The rubber masterbatch according to claim 9 , wherein the tank container is a cylindrical tank container.

Assignments (3)
CORRECTIVE ASSIGNMENT TO CORRECT THE FIRST INVENTOR'S NAME PREVIOUSLY RECORDED AT REEL: 037858 FRAME: 0538. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Mar 18, 2016
From: WANG, MENGJIAO; SONG, JIANJUN; DAI, DEYING
To: EVE RUBBER INSTITUTE CO., LTD.
Reel/Frame 038155/0906 →
CORRECTIVE ASSIGNMENT TO CORRECT THE CITY OF THE RECEIVING PARTY PREVIOUSLY RECORDED AT REEL: 037712 FRAME: 0964. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Feb 19, 2016
From: WANG, MANGJIAO; SONG, JIANJUN; DAI, DEYING
To: EVE RUBBER INSTITUTE CO., LTD.
Reel/Frame 037858/0538 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 11, 2016
From: WANG, MENGJIAO; SONG, JIANJUN; DAI, DEYING
To: EVE RUBBER INSTITUTE CO., LTD.
Reel/Frame 037712/0964 →
Priority Claims (1)
CN 2013 1 0338268 · Aug 5, 2013 · national
Continuity (1)
Related Publication 20160168341A1 · Jun 16, 2016