CN109092188A - A kind of gross rubber production system and production method - Google Patents
A kind of gross rubber production system and production method Download PDFInfo
- Publication number
- CN109092188A CN109092188A CN201811051758.2A CN201811051758A CN109092188A CN 109092188 A CN109092188 A CN 109092188A CN 201811051758 A CN201811051758 A CN 201811051758A CN 109092188 A CN109092188 A CN 109092188A
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- Prior art keywords
- colloid
- powder
- mixed
- unit
- supply unit
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/81—Combinations of similar mixers, e.g. with rotary stirring devices in two or more receptacles
- B01F33/811—Combinations of similar mixers, e.g. with rotary stirring devices in two or more receptacles in two or more consecutive, i.e. successive, mixing receptacles or being consecutively arranged
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/36—Mixing of ingredients for adhesives or glues; Mixing adhesives and gas
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
Abstract
The invention belongs to chemical production technical field more particularly to a kind of gross rubber production system and production methods.The present invention provides a kind of gross rubber production systems, comprising: powder metering supply unit, colloid metering supply unit, mixed cell, filter element and packaging unit；The powder and colloid that mixed cell conveys respectively for mixed powder metering supply unit and colloid metering supply unit；Mixed cell is continuous mixed cell, including mixed zones more than two ranks or two ranks；The input end of filter element is connect with mixed cell, and filtered material is passed to packaging unit.In gross rubber production system of the present invention, mixed cell is continuous mixed cell, including mixed zones more than two ranks or two ranks, when using the gross rubber production system, colloid can be achieved and powder continuous feed, colloid are added to the first rank mixed zone, powder is continuously added to the mixed zone of not same order, rubber compound production efficiency is greatly improved, labor intensity is reduced.
Description
Technical field
The invention belongs to chemical production technical field more particularly to a kind of gross rubber production system and production methods.
Background technique
Currently, rubber compound in process of production, first puts into colloid starting material using traditional blender clearance-type production,
Then it is gradually added powder in batches again, powder could be added after needing the powder that previous batch is added to mix for second and mix
It closes, large labor intensity, production efficiency is low, high production cost.
Summary of the invention
The present invention provides a kind of gross rubber production system and production methods, for solving rubber compound productive labor intensity
Greatly, the problem of production efficiency is low, high production cost.
The specific technical solution of the present invention is as follows:
A kind of gross rubber production system, comprising: powder metering supply unit, colloid measure supply unit, mixed cell, mistake
Filter unit and packaging unit；
The mixed cell is defeated for mixing the powder metering supply unit and colloid metering supply unit difference
The powder and colloid sent；
The mixed cell is continuous mixed cell, including mixed zones more than two ranks or two ranks；
The input end of the filter element is connect with the mixed cell, and filtered material is passed to the packaging
Unit.
Preferably, further includes: cooling unit；
The inlet end and an outlet end of the cooling unit is connect with the filter element and the packaging unit respectively.
Preferably, further includes: control unit；
Described control unit respectively with the powder metering supply unit, colloid metering supply unit, described mix
Unit, the filter element, the cooling unit and packaging unit electrical connection.
Preferably, the filter element is continuous filter element.
Preferably, the cooling unit is continuous coo1ing unit.
The present invention also provides a kind of mixing glue production method, the gross rubber production system by adopting the above technical scheme,
The following steps are included:
Powder and colloid are passed through into the powder metering supply unit respectively and colloid metering supply unit is delivered to
The mixed cell after being mixed, is filtered through the filter element, then is packed in the packaging unit, and rubber compound is obtained；
Wherein, the colloid is added to the first rank mixed zone, and the powder is continuously added to the mixed zone of not same order.
Preferably, through the filter element filter and then the packaging unit packaging before, further includes:
Preset temperature is cooled to by the cooling unit.
Preferably, the powder includes white carbon black powder.
Preferably, the colloid includes raw rubber.
Preferably, the mass ratio of the powder and the colloid is 3~7:7~3.
The present invention provides a kind of gross rubber production systems, comprising: powder metering supply unit, colloid metering conveying are single
Member, mixed cell, filter element and packaging unit；The mixed cell is for mixing the powder metering supply unit and described
The powder and colloid that colloid metering supply unit conveys respectively；The mixed cell is continuous mixed cell, including two ranks or two
Mixed zone more than rank；The input end of the filter element is connect with the mixed cell, and filtered material is passed to
The packaging unit.In gross rubber production system of the present invention, mixed cell is continuous mixed cell, including two ranks or two ranks or more
Mixed zone, using, it can be achieved that colloid and powder continuous feed, colloid is added to the first rank and mixes when the gross rubber production system
Area, powder are continuously added to the mixed zone of not same order, greatly improve rubber compound production efficiency, reduce labor intensity.
Detailed description of the invention
In order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, to embodiment or will show below
There is attached drawing needed in technical description to be briefly described.
Fig. 1 is the flow chart that glue production method is kneaded in the embodiment of the present invention 1.
Specific embodiment
The present invention provides a kind of gross rubber production system and production methods, for solving rubber compound productive labor intensity
Greatly, the problem of production efficiency is low, high production cost.
The technical scheme in the embodiments of the invention will be clearly and completely described below, it is clear that described implementation
Example is only a part of the embodiment of the present invention, instead of all the embodiments.Based on the embodiments of the present invention, this field is common
Technical staff's every other embodiment obtained without making creative work belongs to the model that the present invention protects
It encloses.
A kind of gross rubber production system, comprising: powder metering supply unit, colloid measure supply unit, mixed cell, mistake
Filter unit and packaging unit；
The powder and glue that mixed cell conveys respectively for mixed powder metering supply unit and colloid metering supply unit
Body；
Mixed cell is continuous mixed cell, including mixed zones more than two ranks or two ranks；
The input end of filter element is connect with mixed cell, and filtered material is passed to packaging unit.
In gross rubber production system of the present invention, mixed cell is continuous mixed cell, including more than two ranks or two ranks mixed
Close area, using when the gross rubber production system, it can be achieved that colloid and powder continuous feed, colloid are added to the first rank mixed zone,
Powder is continuously added to the mixed zone of not same order, greatly improves rubber compound production efficiency, reduces labor intensity.
In the present invention, packaging unit can carry out quantitative package.
Further, further includes: cooling unit；
The inlet end and an outlet end of cooling unit is connect with filter element and packaging unit respectively.
In the production process of rubber compound, filtered temperature of charge is higher, but the prior art is used and placed in air
It carries out cooling method and is cooled to the temperature that can be packed, production efficiency is low, high production cost.
Further, further includes: control unit；
Control unit respectively with powder metering supply unit, colloid metering supply unit, mixed cell, filter element, cold
But unit and packaging unit electrical connection.
Control unit of the present invention to powder metering supply unit, colloid metering supply unit, mixed cell, filter element,
Cooling unit and packaging unit carry out automation continuous control, and gross rubber production system can be made to realize fully-automatic production, production effect
Rate greatly improves, and reduces labor intensity.
In the present invention, filter element is continuous filter element.Filter element is provided with supercharger and filter.Supercharger is
Single screw rod structure supercharger, filter material is continuously conveyed into filter, and filter is double-station board plug type filter, replacement
Replaceable station is switched fast when strainer, and realization does not stop continuous filtering.It should be noted that the quantity of supercharger and filter
It can be adjusted, be not specifically limited herein according to actual needs.
In the present invention, cooling unit is continuous coo1ing unit.Continuous coo1ing unit is single screw rod structure cooling unit or double
Screw-rod structure cooling unit, material continuously enter cooling unit, and external jacket is cooling, and inner shaft is cooling, realize in material transportation process
Continuous coo1ing.
Colloid and powder can be directly added by gross rubber production system of the present invention, colloid and powder continuous feed, continuous mixed
Merge continuous discharge, and by continuous filter element and continuous coo1ing unit, then be directly transferred to packaging unit and packed, greatly
It is big to improve production efficiency, reduce labor intensity.Also, gross rubber production system of the present invention can adjust powder by control unit
Body measures the parameter of supply unit, colloid metering supply unit, mixed cell, filter element, cooling unit and packaging unit, very
The hardness of good adjustment rubber compound, it is ensured that rubber compound is met the requirements.
The present invention also provides a kind of mixing glue production method, gross rubber production system by adopting the above technical scheme, including
Following steps:
Powder and colloid are passed through into powder metering supply unit respectively and colloid metering supply unit is delivered to mixed cell,
It after being mixed, filters through filter element, then is packed in packaging unit, obtain rubber compound；
Wherein, colloid is added to the first rank mixed zone, and powder is continuously added to the mixed zone of not same order.
In the present invention, filtered through filter element and then before packaging unit packaging, further includes:
Preset temperature is cooled to by cooling unit.
Preset temperature is the temperature that can be packed.
In the present invention, powder includes white carbon black powder, and white carbon black powder can be one or more.
Colloid includes raw rubber, and raw rubber can be one or more.
The mass ratio of powder and colloid is 3~7:7~3.
The present invention is kneaded glue production method and can continuously be mixed by mixed cell to powder and colloid material, realizes entirely certainly
Dynamic continuous production, ultimately forms the rubber compound met the requirements, and compound manufacture stability is good, and intensity is high, heat resistance is good.This hair
Bright mixing glue production method is realized to the continuous automatic production of rubber compound by mixed cell, is not needed mixed powder in batches
Body and colloid, directly powder and colloid, which can be added in gross rubber production system, can produce rubber compound, substantially increase life
Efficiency is produced, man power and material is saved.Also, the present invention, which is kneaded glue production method, can adjust powder metering by control unit
The parameter of supply unit, colloid metering supply unit, mixed cell, filter element, cooling unit and packaging unit, is adjusted well
The hardness of whole rubber compound, it is ensured that rubber compound is met the requirements.
For a further understanding of the present invention, the present invention will be described in detail combined with specific embodiments below.
Embodiment 1
Referring to Fig. 1, to be kneaded the flow chart of glue production method in the embodiment of the present invention 1.In the present embodiment, powder and glue
The mass ratio of body is 3:7.Powder includes two kinds of white carbon black powders, respectively the first powder and the second powder.First powder and
The mass ratio of two powders respectively enters the first of mixed cell by measuring supply unit for 2:1, the first powder and the second powder
The second-order mixed zone of rank mixed zone and mixed cell.Colloid includes three kinds of raw rubbers, respectively the first colloid, the second colloid and the
Three colloids, the mass ratio of the first colloid, the second colloid and third colloid are 4:2:1, the first colloid, the second colloid and third colloid
Supply unit, which is measured, by colloid enters the first rank mixed zone of mixed cell, in the first rank mixed zone of mixed cell, first
Powder, the first colloid, the second colloid, third colloid are mixed, and material enters the second-order mixed zone of mixed cell after mixing,
It is mixed again with the second powder.
The present embodiment mixed cell is provided with quadravalence mixed zone altogether, by the material of the second-order mixed zone of mixed cell after
It is continuous to be delivered to the third rank mixed zone of mixed cell and the fourth order mixed zone of mixed cell and mixed, so that powder and colloid
Material is mixed thoroughly.Uniformly mixed material is transported in a single screw rod supercharger of continuous filter element, single spiral shell
Uniformly mixed material pressurization is continuously conveyed into the double-station board plug type filter of continuous filter element bar supercharger, realizes
The filtering of material, material by be cooled to after two double-screw structure continuous coo1ing units 50 DEG C hereinafter, by packaging unit into
Row quantitative package obtains finished product rubber compound.
Embodiment 2
In the present embodiment, the mass ratio of powder and colloid is 5:5.Powder include three kinds of white carbon black powders, respectively first
Powder, the second powder and third powder.The mass ratio of first powder, the second powder and third powder be 5:3:2, the first powder,
Second powder and third powder by measure supply unit respectively enter the first rank mixed zone of mixed cell, mixed cell the
The third rank mixed zone of second order mixed zone and mixed cell.Colloid include three kinds of raw rubbers, respectively the first colloid, the second colloid and
Third colloid, the mass ratio of the first colloid, the second colloid and third colloid are 2:2:1, the first colloid, the second colloid and third glue
Body measures supply unit by colloid and enters the first rank mixed zone of mixed cell, in the first rank mixed zone of mixed cell, the
One powder, the first colloid, the second colloid, third colloid are mixed, in the first mixed object in rank mixed zone of mixed cell
Material enters the second-order mixed zone of mixed cell, is mixed with the second powder, mixes in the second-order mixed zone of mixed cell
Material afterwards enters the third rank mixed zone of mixed cell, is mixed with third powder.
The present embodiment mixed cell is provided with totally five rank mixed zone, by the material of the third rank mixed zone of mixed cell after
It is continuous to be delivered to the fourth order mixed zone of mixed cell and the 5th rank mixed zone of mixed cell and mixed, so that powder and colloid
Material is mixed thoroughly.Uniformly mixed material is transported in a single screw rod supercharger of continuous filter element, single spiral shell
Uniformly mixed material pressurization is continuously conveyed into the double-station board plug type filter of continuous filter element bar supercharger, realizes
The filtering of material, material by be cooled to after two double-screw structure continuous coo1ing units 50 DEG C hereinafter, by packaging unit into
Row quantitative package obtains finished product rubber compound.
The above is only a preferred embodiment of the present invention, it is noted that for the ordinary skill people of the art
For member, various improvements and modifications may be made without departing from the principle of the present invention, these improvements and modifications are also answered
It is considered as protection scope of the present invention.
Claims (10)
1. a kind of gross rubber production system characterized by comprising powder metering supply unit, mixes colloid metering supply unit
Close unit, filter element and packaging unit；
The mixed cell is used to mix the powder metering supply unit and the colloid measures what supply unit conveyed respectively
Powder and colloid；
The mixed cell is continuous mixed cell, including mixed zones more than two ranks or two ranks；
The input end of the filter element is connect with the mixed cell, and filtered material is passed to the packing list
Member.
2. gross rubber production system according to claim 1, which is characterized in that further include: cooling unit；
The inlet end and an outlet end of the cooling unit is connect with the filter element and the packaging unit respectively.
3. gross rubber production system according to claim 2, which is characterized in that further include: control unit；
Described control unit respectively with the powder metering supply unit, the colloid metering supply unit, the mixed cell,
The filter element, the cooling unit and packaging unit electrical connection.
4. gross rubber production system according to claim 2, which is characterized in that the filter element is that continuous filtering is single
Member.
5. gross rubber production system according to claim 2, which is characterized in that the cooling unit is continuous coo1ing list
Member.
6. a kind of mixing glue production method, which is characterized in that be kneaded using described in claim 2 to claim 5 any one
Glue production system, comprising the following steps:
By powder and colloid pass through the powder metering supply unit respectively and colloid metering supply unit be delivered to it is described
Mixed cell after being mixed, is filtered through the filter element, then is packed in the packaging unit, and rubber compound is obtained；
Wherein, the colloid is added to the first rank mixed zone, and the powder is continuously added to the mixed zone of not same order.
7. mixing glue production method according to claim 6, which is characterized in that filtered through the filter element and then
Before packaging unit packaging, further includes:
Preset temperature is cooled to by the cooling unit.
8. mixing glue production method according to claim 7, which is characterized in that the powder includes white carbon black powder.
9. mixing glue production method according to claim 7, which is characterized in that the colloid includes raw rubber.
10. mixing glue production method according to claim 7, which is characterized in that the quality of the powder and the colloid
Than for 3~7:7~3.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811051758.2A CN109092188A (en) | 2018-09-10 | 2018-09-10 | A kind of gross rubber production system and production method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811051758.2A CN109092188A (en) | 2018-09-10 | 2018-09-10 | A kind of gross rubber production system and production method |
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| Publication Number | Publication Date |
|---|---|
| CN109092188A true CN109092188A (en) | 2018-12-28 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201811051758.2A Pending CN109092188A (en) | 2018-09-10 | 2018-09-10 | A kind of gross rubber production system and production method |
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Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06313046A (en) * | 1993-04-27 | 1994-11-08 | Toray Dow Corning Silicone Co Ltd | Continuous production of thermally curing type silicon rubber compound |
| CN1693368A (en) * | 2005-07-21 | 2005-11-09 | 江苏宏达化工新材料股份有限公司 | Process for preparing special material for injecting forming composite silicon rubber insulator mixing refine rubber |
| CN102120345A (en) * | 2011-01-25 | 2011-07-13 | 青岛科技大学 | Blocky rubber continuous mixing method and device |
| CN202200526U (en) * | 2011-08-23 | 2012-04-25 | 常州市晨光机械制造有限公司 | Double-station filter |
| CN103012870A (en) * | 2012-12-20 | 2013-04-03 | 青岛科技大学 | Modified carcass ply compound of all-steel radial tire |
| CN105965716A (en) * | 2016-04-28 | 2016-09-28 | 广州市白云化工实业有限公司 | Continuous production process and device for rubber compound |
| CN107234743A (en) * | 2017-06-15 | 2017-10-10 | 安徽世界村新材料有限公司 | A kind of regenerating waste or used rubber gross rubber production system |
-
2018
- 2018-09-10 CN CN201811051758.2A patent/CN109092188A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06313046A (en) * | 1993-04-27 | 1994-11-08 | Toray Dow Corning Silicone Co Ltd | Continuous production of thermally curing type silicon rubber compound |
| CN1693368A (en) * | 2005-07-21 | 2005-11-09 | 江苏宏达化工新材料股份有限公司 | Process for preparing special material for injecting forming composite silicon rubber insulator mixing refine rubber |
| CN102120345A (en) * | 2011-01-25 | 2011-07-13 | 青岛科技大学 | Blocky rubber continuous mixing method and device |
| CN202200526U (en) * | 2011-08-23 | 2012-04-25 | 常州市晨光机械制造有限公司 | Double-station filter |
| CN103012870A (en) * | 2012-12-20 | 2013-04-03 | 青岛科技大学 | Modified carcass ply compound of all-steel radial tire |
| CN105965716A (en) * | 2016-04-28 | 2016-09-28 | 广州市白云化工实业有限公司 | Continuous production process and device for rubber compound |
| CN107234743A (en) * | 2017-06-15 | 2017-10-10 | 安徽世界村新材料有限公司 | A kind of regenerating waste or used rubber gross rubber production system |
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Application publication date: 20181228 |