CN107266744A - A kind of sulfuration process of rubber - Google Patents
A kind of sulfuration process of rubber Download PDFInfo
- Publication number
- CN107266744A CN107266744A CN201710707101.6A CN201710707101A CN107266744A CN 107266744 A CN107266744 A CN 107266744A CN 201710707101 A CN201710707101 A CN 201710707101A CN 107266744 A CN107266744 A CN 107266744A
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- rubber
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L9/00—Compositions of homopolymers or copolymers of conjugated diene hydrocarbons
- C08L9/06—Copolymers with styrene
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/002—Methods
- B29B7/005—Methods for mixing in batches
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C35/00—Heating, cooling or curing, e.g. crosslinking or vulcanising; Apparatus therefor
- B29C35/02—Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/18—Oxygen-containing compounds, e.g. metal carbonyls
- C08K3/20—Oxides; Hydroxides
- C08K3/22—Oxides; Hydroxides of metals
- C08K2003/2296—Oxides; Hydroxides of metals of zinc
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K2201/00—Specific properties of additives
- C08K2201/014—Additives containing two or more different additives of the same subgroup in C08K
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2205/00—Polymer mixtures characterised by other features
- C08L2205/02—Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2205/00—Polymer mixtures characterised by other features
- C08L2205/03—Polymer mixtures characterised by other features containing three or more polymers in a blend
- C08L2205/035—Polymer mixtures characterised by other features containing three or more polymers in a blend containing four or more polymers in a blend
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
Abstract
The invention discloses a kind of sulfuration process of rubber, by butadiene-styrene rubber, cis-butadiene cement, zinc oxide, stearic acid, antioxidant 4010NA, anti-aging agent RD, antioxidant d, captax, altax, paraffin, coumarone, carbon black N330, carbon black N660, machine oil, it is according to mass percent proportioning, 65:32:4.6:1.8:0.9:0.9:0.8:0.7:1.2:0.5:5:38:20:18, after mixing, add in banbury and knead, the melting temperature for controlling banbury is 40~80 DEG C, and mixing time is 10~20min, and the film after mixing is placed into 2~24h, then cut-parts are vulcanized, the present invention is for the problem of presence, devising the sulfuration process composition of rubber, and using the sulfuration process environmental protection and energy saving of the rubber of composition preparation, step is simple and cost is relatively low.
Description
Technical field
The invention belongs to the technical field of rubber, specially a kind of sulfuration process of rubber.
Background technology
The rubber of early stage is taken from flexible, the insulation being made after the latex of the plants such as rubber tree, kok-saghyz, processing
Property, the material of impermeable water and air.Elastomeric high-molecular compound.It is divided into two kinds of natural rubber and synthetic rubber.Natural rubber
Glue is made of the extraction colloid post-processing from the plants such as rubber tree, kok-saghyz;Synthetic rubber is then by the aggregated reaction of various monomers
And obtain.Rubber is widely used in all aspects of industry or life.
Rubber needs sulfidation in production process, and a kind of rational technique can improve rubber quality.
The content of the invention
It is an object of the invention to provide a kind of sulfuration process of rubber, cost is reduced, environmental protection is handy.
In order to solve the above-mentioned technical problem, the technical solution adopted by the present invention is:
A kind of sulfuration process of rubber, comprises the following steps:
(1) by butadiene-styrene rubber, cis-butadiene cement, zinc oxide, stearic acid, antioxidant 4010NA, anti-aging agent RD, antioxidant d, promotion
Agent M, altax, paraffin, coumarone, carbon black N330, carbon black N660, machine oil, be according to mass percent proportioning, 65:32:
4.6:1.8:0.9:0.9:0.8:0.7:1.2:0.5:5:38:20:18, after mixing, add in banbury and knead, control banbury
Melting temperature be 40~80 DEG C, mixing time is 10~20min, the film after mixing is placed into 2~24h, then cut-parts enter
Row vulcanization;
(2) curing temperature is adjusted to 180~200 DEG C, and controls plate temperature to be 110~120 DEG C, be allowed to constant;
(3) mould is placed on closure flat board and be preheated within the scope of defined curing temperature ± 1 DEG C, and at such a temperature
Keep 20~30min;
(4) when vulcanizer works, sulfide stress is provided by pump, pressure is adjusted to 25MPa by pressure-regulating valve;
(5) compound blank is quickly put into preheated mould, immediately matched moulds, is placed in flat board center, up and down each layer vulcanizing mold
Type is aligned with the after-applied pressure in same orientation, flat board is increased, when pressure gauge indicates to arrive 15MPa, appropriate release exhaust 3~4
It is secondary, then pressure is reached 25MPa, start to calculate cure time, reaching scheduled time pressure release immediately in vulcanization opens mould, takes out examination
Sample;
(6) sample shear after vulcanizing is removed photoresist side, and performance test is carried out after placing 10~13h at room temperature.
Further, elastomeric compound is examined:Test is sampled to the elastomeric compound after mixing, method and test value are according to as follows
Procedure and numerical value are carried out, and choose the qualified elastomeric compound of whole test values:
A, tested using Shore A durometer, qualified Shore A hardness value scope:63±3;
B, tested using puller system, tensile strength number range:≥15MPa;
C, tested using puller system, elongation at break number range:>=400%;
D, use puller system, Shore A durometer test, heat ageing number range:Firmness change (HS) 15%MAX, stretching
Change rate of strength 25%MAX, elongation percentage rate of change 25%MAX;
E, use special fixtures, baking oven test, compression set number range.
The beneficial effects of the invention are as follows:
The present invention is directed to the problem of existing, and devises the sulfuration process composition of rubber, the rubber prepared using the composition
Sulfuration process environmental protection and energy saving, step is simple and cost is relatively low.
Embodiment
Embodiments of the invention are described in detail below, but what the present invention can be defined by the claims and cover
Multitude of different ways is implemented.
A kind of sulfuration process of rubber, comprises the following steps:
(1) knead:By butadiene-styrene rubber, cis-butadiene cement, zinc oxide, stearic acid, antioxidant 4010NA, anti-aging agent RD, antioxidant d,
Captax, altax, paraffin, coumarone, carbon black N330, carbon black N660, machine oil, be according to mass percent proportioning, 65:
32:4.6:1.8:0.9:0.9:0.8:0.7:1.2:0.5:5:38:20:18, after mixing, add in banbury and knead, control close
The melting temperature of mill is 40~80 DEG C, and mixing time is 10~20min, and the film after mixing is placed into 2~24h, then cut out
Piece is vulcanized;
(2) curing temperature is adjusted to 180~200 DEG C, and controls plate temperature to be 110~120 DEG C, be allowed to constant;
(3) mould is placed on closure flat board and be preheated within the scope of defined curing temperature ± 1 DEG C, and at such a temperature
Keep 20~30min;
(4) when vulcanizer works, sulfide stress is provided by pump, pressure is adjusted to 25MPa by pressure-regulating valve;
(5) compound blank is quickly put into preheated mould, immediately matched moulds, is placed in flat board center, up and down each layer vulcanizing mold
Type is aligned with the after-applied pressure in same orientation, flat board is increased, when pressure gauge indicates to arrive 15MPa, appropriate release exhaust 3~4
It is secondary, then pressure is reached 25MPa, start to calculate cure time, reaching scheduled time pressure release immediately in vulcanization opens mould, takes out examination
Sample;
(6) sample shear after vulcanizing is removed photoresist side, and performance test is carried out after placing 10~13h at room temperature.
Elastomeric compound is examined:It is sampled test to the elastomeric compound after mixing, method and test value process as follows
Carried out with numerical value, and choose the qualified elastomeric compound of whole test values:
A, tested using Shore A durometer, qualified Shore A hardness value scope:63±3;
B, tested using puller system, tensile strength number range:≥15MPa;
C, tested using puller system, elongation at break number range:>=400%;
D, use puller system, Shore A durometer test, heat ageing number range:Firmness change (HS) 15%MAX, stretching
Change rate of strength 25%MAX, elongation percentage rate of change 25%MAX;
E, use special fixtures, baking oven test, compression set number range.
Using the sulfuration process environmental protection and energy saving of the rubber of composition preparation, step is simple and cost is relatively low.
The embodiments of the present invention described above are not intended to limit the scope of the present invention, any in the present invention
Spirit and principle within the modifications, equivalent substitutions and improvements made etc., should be included in the claim protection model of the present invention
Within enclosing.
Claims (2)
1. a kind of sulfuration process of rubber, it is characterised in that comprise the following steps:
(1) by butadiene-styrene rubber, cis-butadiene cement, zinc oxide, stearic acid, antioxidant 4010NA, anti-aging agent RD, antioxidant d, captax,
Altax, paraffin, coumarone, carbon black N330, carbon black N660, machine oil, be according to mass percent proportioning, 65:32:4.6:
1.8:0.9:0.9:0.8:0.7:1.2:0.5:5:38:20:18, after mixing, add in banbury and knead, control the mixed of banbury
It is 40~80 DEG C to refine temperature, and mixing time is 10~20min, and the film after mixing is placed into 2~24h, and then cut-parts carry out sulphur
Change;
(2) curing temperature is adjusted to 180~200 DEG C, and controls plate temperature to be 110~120 DEG C, be allowed to constant;
(3) mould is placed on closure flat board and be preheated within the scope of defined curing temperature ± 1 DEG C, and kept at such a temperature
20~30min;
(4) when vulcanizer works, sulfide stress is provided by pump, pressure is adjusted to 25MPa by pressure-regulating valve;
(5) compound blank is quickly put into preheated mould, immediately matched moulds, is placed in flat board center, up and down each layer sulfide model pair
Just in the after-applied pressure in same orientation, flat board is set to increase, when pressure gauge indicates to arrive 15MPa, appropriate release is vented 3~4 times, so
After pressure is reached 25MPa, start to calculate cure time, reaching scheduled time pressure release immediately in vulcanization opens mould, takes out sample;
(6) sample shear after vulcanizing is removed photoresist side, and performance test is carried out after placing 10~13h at room temperature.
2. the sulfuration process of rubber according to claim 1, it is characterised in that elastomeric compound is examined:To the mixing after mixing
Glue is sampled test, and process and numerical value are carried out as follows for method and test value, and it is qualified to choose whole test values
Elastomeric compound:
A, tested using Shore A durometer, qualified Shore A hardness value scope:63±3;
B, tested using puller system, tensile strength number range:≥15MPa;
C, tested using puller system, elongation at break number range:>=400%;
D, use puller system, Shore A durometer test, heat ageing number range:Firmness change (HS) 15%MAX, tensile strength
Rate of change 25%MAX, elongation percentage rate of change 25%MAX;
E, use special fixtures, baking oven test, compression set number range.
Priority Applications (1)
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CN201710707101.6A CN107266744A (en) | 2017-08-17 | 2017-08-17 | A kind of sulfuration process of rubber |
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CN201710707101.6A CN107266744A (en) | 2017-08-17 | 2017-08-17 | A kind of sulfuration process of rubber |
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CN107266744A true CN107266744A (en) | 2017-10-20 |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112406129A (en) * | 2020-10-29 | 2021-02-26 | 清华大学 | Production method and production system of rubber part |
CN116903941A (en) * | 2023-07-14 | 2023-10-20 | 宁国中奕橡塑有限公司 | One-time molding vulcanization process for rubber products |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102786745A (en) * | 2012-08-24 | 2012-11-21 | 无锡圣丰减震器有限公司 | Production process for tire curing bladders |
CN102786746A (en) * | 2012-08-24 | 2012-11-21 | 无锡圣丰减震器有限公司 | Tire vulcanizing capsule |
CN106378893A (en) * | 2016-08-31 | 2017-02-08 | 柳州元吉兴工业技术有限公司 | Rubber vulcanization process |
-
2017
- 2017-08-17 CN CN201710707101.6A patent/CN107266744A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102786745A (en) * | 2012-08-24 | 2012-11-21 | 无锡圣丰减震器有限公司 | Production process for tire curing bladders |
CN102786746A (en) * | 2012-08-24 | 2012-11-21 | 无锡圣丰减震器有限公司 | Tire vulcanizing capsule |
CN106378893A (en) * | 2016-08-31 | 2017-02-08 | 柳州元吉兴工业技术有限公司 | Rubber vulcanization process |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112406129A (en) * | 2020-10-29 | 2021-02-26 | 清华大学 | Production method and production system of rubber part |
CN112406129B (en) * | 2020-10-29 | 2021-11-30 | 清华大学 | Production method and production system of rubber part |
CN116903941A (en) * | 2023-07-14 | 2023-10-20 | 宁国中奕橡塑有限公司 | One-time molding vulcanization process for rubber products |
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Application publication date: 20171020 |
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