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US4374941A Expired / Lapsed US ⏱️ 0.0 years remaining

Particle size control of SBR/carbon black powder

Assignee: Goodyear Tire and Rubber Co
•
Filing: 1981-08-27
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Granted: 1983-02-22
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Expires: 2001-08-27
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Abstract

Abstract There is disclosed a process for the production of tack-free, pourable, filler containing elastomer powder which comprises (a) dispersing a carbon black filler in water; (b) mixing the thus dispersed carbon black filler with an elastomer latex; (c) coagulating the thus produced mixture of elastomer latex and carbon black with a two-stage coagulation solution; (d) partitioning the thus coagulated suspension with a coating resin; and (e) filtering, washing and drying of the resultant powder, the improvement comprising using as a coating resin a mixture of a styrene/butadiene resin and a styrene/α-methylstyrene or a polystyrene resin wherein the weight ratio of the styrene/butadiene resin to the styrene/α-methylstyrene or polystyrene resin ranges between 4/1 and 1/4, said resins containing a mixture of added surfactants, the first being sodium lauryl sulfate and the second being a nonionic isooctyl phenoxy polyethoxy ethanol which contains 10 moles of ethylene oxide in the polyethoxy portion thereof, said mixture of surfactants being added in an amount at least 4 percent by weight and being in a weight ratio of sodium lauryl sulfate to the nonionic surfactant ranging from 2/1 to 1/2, and wherein the coagulation temperature ranges from 70° to 90° C., and a further improvement of using the coagulating step in (c) a two-step coagulating process, the first being acid/salt and then next using an acid/alum coagulating solution.

Inventors

  • 👤 Paul H. Sandstrom

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 11:12
CPC Classifications
C; C08; C08J; C08J3/00; C08J3/12; C08J3/124; C08J3/20; C08J3/205; C08J3/21; C08J3/215; C08K; C08K3/00; C08K3/02; C08K3/04; C08J2321/00; Y; Y10; Y10S; Y10S524/00; Y10S524/904

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 371 words
A process for the production of tack-free, pourable, filler containing elastomer powder which comprises (a) dispersing a reinforcing type carbon black filler in water, said carbon black being selected from the group consisting of high abrasion furnace (HAF), intermediate super abrasion fuurnace (ISAF), and fast extrusion furnace (FEF), (b) mixing the thus dispersed carbon black filler with an elastomer latex, said latex being selected from the group of styrene/butadiene rubbers, acrylonitrile/butadiene rubbers, polypropylene rubbers, polybutadiene rubbers, polyisoprene rubbers, and copolymers of dimethyl butadiene/butadiene rubbers, the improvement comprising (c) coagulating the thus produced mixture of elastomer latex and carbon black with a two-stage coagulating process, comprising first coagulating the mixture of elastomer latex and carbon black by the use of a dilute salt/acid solution at a pH 3-5, at temperatures varying from 30 to 90° C. wherein the concentration of salt varies between 2-20 parts per hundred of rubber, and the concentration of the salt in the solution may vary between 0.1 and 1.0 percent, and then conducting the second stage coagulation of the mixture by adding sufficient alum to give a concentration of 1 to 10 parts of alum per 100 parts of rubber, adjusting the pH of the mixture to a pH of 2 to 3 with dilute sulfuric acid, (d) partitioning the thus coagulated suspension with a coating resin by adding a dilute solution of a coating resin to the coagulated particles formed during the first stage coagulation while maintaining the temperature between 70° C. and 90° C. and (e) filtering, washing and drying the resultant powder dispersion, an additional improvement comprising using as a coating resin a mixture of a styrene/butadiene resin and a styrene/α-methylstyrene or a polystyrene resin wherein the weight ratio of the styrene/butadiene resin to the styrene/α-methylstyrene or polystyrene resin ranges between 4/1 and 1/4, said resins containing a mixture of added surfactants, the first being sodium lauryl sulfate and the second being a nonionic isooctyl phenoxy polyethoxy ethanol which contains 10 moles of ethylene oxide in the polyethoxy portion thereof, said mixture of surfactants being added in an amount at least 4 percent by weight and being in a weight ratio of sodium lauryl sulfate to the nonionic surfactant ranging from 2/1 to 1/2.
Claim 2
Dependent Claim 371 words
A process for the production of tack-free, pourable, filler containing elastomer powder which comprises (a) dispersing a reinforcing type carbon black filler in water, said carbon black being selected from the group consisting of high abrasion furnace (HAF), intermediate super abrasion fuurnace (ISAF), and fast extrusion furnace (FEF), (b) mixing the thus dispersed carbon black filler with an elastomer latex, said latex being selected from the group of styrene/butadiene rubbers, acrylonitrile/butadiene rubbers, polypropylene rubbers, polybutadiene rubbers, polyisoprene rubbers, and copolymers of dimethyl butadiene/butadiene rubbers, the improvement comprising (c) coagulating the thus produced mixture of elastomer latex and carbon black with a two-stage coagulating process, comprising first coagulating the mixture of elastomer latex and carbon black by the use of a dilute salt/acid solution at a pH 3-5, at temperatures varying from 30 to 90° C. wherein the concentration of salt varies between 2-20 parts per hundred of rubber, and the concentration of the salt in the solution may vary between 0.1 and 1.0 percent, and then conducting the second stage coagulation of the mixture by adding sufficient alum to give a concentration of 1 to 10 parts of alum per 100 parts of rubber, adjusting the pH of the mixture to a pH of 2 to 3 with dilute sulfuric acid, (d) partitioning the thus coagulated suspension with a coating resin by adding a dilute solution of a coating resin to the coagulated particles formed during the first stage coagulation while maintaining the temperature between 70° C. and 90° C. and (e) filtering, washing and drying the resultant powder dispersion, an additional improvement comprising using as a coating resin a mixture of a styrene/butadiene resin and a styrene/α-methylstyrene or a polystyrene resin wherein the weight ratio of the styrene/butadiene resin to the styrene/α-methylstyrene or polystyrene resin ranges between 4/1 and 1/4, said resins containing a mixture of added surfactants, the first being sodium lauryl sulfate and the second being a nonionic isooctyl phenoxy polyethoxy ethanol which contains 10 moles of ethylene oxide in the polyethoxy portion thereof, said mixture of surfactants being added in an amount at least 4 percent by weight and being in a weight ratio of sodium lauryl sulfate to the nonionic surfactant ranging from 2/1 to 1/2.
Claim 3
Dependent Claim 40 words
A process according to claim 1 wherein the carbon black is prepared using a purified free acid pine lignin dispersant in an amount which is 3 to 6 percent by weight concentration based on the weight of the carbon black.
Claim 4
Dependent Claim 38 words
A process according to claim 1 in which the styrene/butadiene resin contains a styrene to butadiene weight ratio ranging from 75/25 to 95/5 and the styrene/α-methylstyrene resin contains a styrene to α-methylstyrene weight ratio of 99/1 to 50/50.
Claim 5
Dependent Claim 38 words
A process according to claim 2 in which the styrene/butadiene resin contains a styrene to butadiene weight ratio ranging from 75/25 to 95/5 and the styrene/α-methylstyrene resin contains a styrene to α-methylstyrene weight ratio of 99/1 to 50/50.
Claim 6
Dependent Claim 32 words
A process according to claim 1 wherein the styrene/butadiene resin has a styrene to butadiene weight ratio of 90/10 and the styrene/α-methylstyrene resin has a styrene to α-methylstyrene weight ratio of 75/25.
Claim 7
Dependent Claim 32 words
A process according to claim 2 wherein the styrene/butadiene resin has a styrene to butadiene with ratio of 90/10 and the styrene/α-methylstyrene resin has a styrene to α-methylstyrene weight ratio of 75/25.
Claim 8
Dependent Claim 26 words
A process according to claim 1 in which the styrene/butadiene resin contains a styrene to butadiene weight ratio of 95/5 and the second resin is polystyrene.
Claim 9
Dependent Claim 26 words
A process according to claim 2 in which the styrene/butadiene resin contains a styrene to butadiene weight ratio of 95/5 and the second resin is polystyrene.
Claim 10
Dependent Claim 21 words
As the composition the tack-free, pourable, filler containing elastomer powder which is prepared in accordance with the process of claim 1.

References Cited (Backward Citations)

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US3929707A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-02-21 1986-08-23 1987-02-22 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-02-21 1990-08-23 1991-02-22 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-02-21 1994-08-23 1995-02-22 $7700.00 Window Closed / Lapsed

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