Process for producing wet rubber masterbatch, wet rubber masterbatch, and rubber composition containing wet rubber masterbatch
US-2017152353-A1 · Jun 1, 2017 · US
US11230046B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11230046-B2 |
| Application number | US-201716346241-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 18, 2017 |
| Priority date | Jan 10, 2017 |
| Publication date | Jan 25, 2022 |
| Grant date | Jan 25, 2022 |
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An extruder is disclosed including: a barrel; and a screw provided with a helical groove; wherein the screw comprises a dewatering portion comprising a first portion, and a second portion at a location downstream from the first portion; wherein, at the dewatering portion, clearance between the groove and the barrel decreases as one proceeds downstream; and wherein clearance reduction ratio at the first portion is greater than clearance reduction ratio at the second portion.
Opening claim text (preview).
The invention claimed is: 1. An extruder for manufacturing masterbatch comprising: a barrel; and a screw provided with a helical groove; wherein the screw comprises a dewatering portion comprising a first portion, and a second portion at a location downstream from the first portion; wherein, at the dewatering portion, clearance between the groove and the barrel decreases as one proceeds downstream; wherein a reduction ratio R of the clearance at the first portion is greater than a reduction ratio r of the clearance at the second portion; wherein R is given by Formula I; wherein the Formula I is R=H N /H N+1 ; H N indicates the clearance between the groove and the barrel at an arbitrary Nth turn of the groove in the first portion; H N+1 indicates the clearance between the groove and the barrel at an N+1st turn of the groove in the first portion; wherein r is given by Formula II; wherein the Formula II is r=h n /h n+1 ; wherein h n indicates the clearance between the groove and the barrel at an arbitrary nth turn of the groove in the second portion; and wherein h n+1 indicates the clearance between the groove and the barrel at an n+1st turn of the groove. 2. A masterbatch manufacturing method comprising: an operation in which pre-coagulation rubber latex comprising filler is coagulated to obtain a coagulum; and an operation in which the extruder according to claim 1 is used to dewater the coagulum. 3. A tire manufacturing method comprising: an operation in which the masterbatch manufacturing method according to claim 2 is used to prepare a masterbatch; an operation in which at least the masterbatch and compounding ingredients are dry-mixed to obtain a mixture; an operation in which at least a vulcanizing compounding ingredient is kneaded into the mixture to obtain a rubber composition; and an operation in which a green tire equipped with a tire member made up of the rubber composition is made. 4. The tire manufacturing method according to claim 3 wherein the vulcanizing compounding ingredient comprises sulfur. 5. The masterbatch manufacturing method according to claim 2 wherein the operation in which the extruder is used to dewater the coagulum comprises increasing temperature of the coagulum to 110° C. to 160° C. at the first portion. 6. The masterbatch manufacturing method according to claim 2 wherein, during the operation in which the extruder is used to dewater the coagulum, temperature of the coagulum when in a space between the barrel and the second portion of the screw is not greater than 160° C. 7. The masterbatch manufacturing method according to claim 2 further comprising an operation in which a carbon black slurry and rubber latex are mixed to obtain the pre-coagulation rubber latex. 8. The masterbatch manufacturing method according to claim 7 wherein the rubber latex is natural rubber latex. 9. The masterbatch manufacturing method according to claim 2 wherein the operation in which the extruder is used to dewater the coagulum comprises increasing temperature of the coagulum to 110° C. to 160° C. at the first portion; and wherein, during the operation in which the extruder is used to dewater the coagulum, temperature of the coagulum when in a space between the barrel and the second portion of the screw is not greater than 160° C. 10. The masterbatch manufacturing method according to claim 3 , wherein the vulcanizing compounding ingredient is a vulcanizing accelerator selected from the group consisting of a sulfenamide vulcanization accelerator, a thiuram vulcanization accelerator, a thiazole vulcanization accelerator, a thiourea vulcanization accelerator, a guanidine vulcanization accelerator and a dithiocarbamate vulcanization accelerator. 11. The masterbatch manufacturing method according to claim 3 , wherein the vulcanizing compounding ingredient is an organic peroxide.
Coagulation · CPC title
in screw extruders · CPC title
using masterbatch techniques · CPC title
and solid additives · CPC title
Fillers or reinforcements {, e.g. fibres} · CPC title
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