CN104786381B - The process units and its method that a kind of liquid rubber is kneaded - Google Patents
The process units and its method that a kind of liquid rubber is kneaded Download PDFInfo
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- CN104786381B CN104786381B CN201510167656.7A CN201510167656A CN104786381B CN 104786381 B CN104786381 B CN 104786381B CN 201510167656 A CN201510167656 A CN 201510167656A CN 104786381 B CN104786381 B CN 104786381B
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- 229920001971 elastomer Polymers 0.000 title claims abstract description 52
- 239000005060 rubber Substances 0.000 title claims abstract description 52
- 239000007788 liquid Substances 0.000 title claims abstract description 34
- 238000000034 method Methods 0.000 title claims abstract description 31
- 230000008569 process Effects 0.000 title claims abstract description 23
- 239000000839 emulsion Substances 0.000 claims abstract description 39
- 230000015271 coagulation Effects 0.000 claims abstract description 35
- 238000005345 coagulation Methods 0.000 claims abstract description 35
- 238000002156 mixing Methods 0.000 claims abstract description 33
- 230000003068 static effect Effects 0.000 claims abstract description 31
- 239000003292 glue Substances 0.000 claims abstract description 30
- 238000003860 storage Methods 0.000 claims abstract description 22
- 238000001125 extrusion Methods 0.000 claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 13
- 238000003892 spreading Methods 0.000 claims abstract description 12
- 230000007480 spreading Effects 0.000 claims abstract description 12
- 239000003610 charcoal Substances 0.000 claims abstract description 8
- 239000003795 chemical substances by application Substances 0.000 claims description 54
- 230000001804 emulsifying effect Effects 0.000 claims description 52
- 229920000126 latex Polymers 0.000 claims description 41
- 239000004816 latex Substances 0.000 claims description 41
- 239000006229 carbon black Substances 0.000 claims description 38
- 238000006073 displacement reaction Methods 0.000 claims description 22
- 238000001035 drying Methods 0.000 claims description 19
- 150000001875 compounds Chemical class 0.000 claims description 17
- 238000004945 emulsification Methods 0.000 claims description 15
- 238000012545 processing Methods 0.000 claims description 13
- 239000002994 raw material Substances 0.000 claims description 13
- 238000005303 weighing Methods 0.000 claims description 13
- 239000004576 sand Substances 0.000 claims description 6
- 210000000481 breast Anatomy 0.000 claims description 5
- 230000005540 biological transmission Effects 0.000 claims description 3
- 239000012528 membrane Substances 0.000 claims description 3
- 230000002572 peristaltic effect Effects 0.000 claims description 3
- 230000008859 change Effects 0.000 claims description 2
- 230000018044 dehydration Effects 0.000 claims description 2
- 238000006297 dehydration reaction Methods 0.000 claims description 2
- 238000000227 grinding Methods 0.000 claims description 2
- 241000487918 Acacia argyrodendron Species 0.000 abstract description 7
- 235000011222 chang cao shi Nutrition 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 6
- 239000006185 dispersion Substances 0.000 abstract description 5
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 229920003008 liquid latex Polymers 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 239000000047 product Substances 0.000 description 13
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 7
- 239000012744 reinforcing agent Substances 0.000 description 6
- 239000004615 ingredient Substances 0.000 description 5
- 238000004073 vulcanization Methods 0.000 description 4
- 230000006378 damage Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000000375 suspending agent Substances 0.000 description 3
- 244000043261 Hevea brasiliensis Species 0.000 description 2
- 239000004902 Softening Agent Substances 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 2
- -1 age resistor Substances 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 229920003052 natural elastomer Polymers 0.000 description 2
- 229920001194 natural rubber Polymers 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- 230000008023 solidification Effects 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 1
- 229920000715 Mucilage Polymers 0.000 description 1
- 239000010022 Myron Substances 0.000 description 1
- 241001439614 Myron Species 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 238000007605 air drying Methods 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- ZPUCINDJVBIVPJ-LJISPDSOSA-N ***e Chemical compound O([C@H]1C[C@@H]2CC[C@@H](N2C)[C@H]1C(=O)OC)C(=O)C1=CC=CC=C1 ZPUCINDJVBIVPJ-LJISPDSOSA-N 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
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- 239000002283 diesel fuel Substances 0.000 description 1
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- 239000002270 dispersing agent Substances 0.000 description 1
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- 239000004744 fabric Substances 0.000 description 1
- 229920005570 flexible polymer Polymers 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 230000009969 flowable effect Effects 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000010074 rubber mixing Methods 0.000 description 1
- 238000010057 rubber processing Methods 0.000 description 1
- 239000011265 semifinished product Substances 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 229920003051 synthetic elastomer Polymers 0.000 description 1
- 239000005061 synthetic rubber Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
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- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
Abstract
The process units and its method being kneaded the invention discloses a kind of liquid rubber.The batch mixing output device (2) of the process units includes spreading extrusion die (26), coagulation rubber extruding machine (27), coagulation glue storage tank (28) and static mixer (29)；The upper end of the coagulation glue storage tank is connected with static mixer, and its lower end is connected with coagulation rubber extruding machine；The right-hand member of the coagulation rubber extruding machine is connected with spreading extrusion die.The production method of the liquid rubber, mixed emulsion enters static mixer at a high speed with the black emulsion of black wood charcoal, moment mixing, enter coagulation glue storage tank after condensing, the coagulation glue of piece banding is extruded into by spreading extrusion die, enter after finally being squeezed the water out by dewaterer in microwave drier, output obtains qualified products.Energy consumption of the invention is small, pollution is small, can make black wood charcoal is black to have good dispersion effect in liquid latex, the rubber produced has the excellent combination property such as high resiliency, soft, high maximum elongation and high tensile.
Description
Technical field
The present invention relates to rubber processing, and in particular to the process units and its method that a kind of liquid rubber is kneaded.
Background technology
Rubber is a kind of flexible polymer.Rubber can obtain or artificial from the myron of some plants
, both considerable application and products, such as tire, packing ring etc., then as Important Economic crop.Rubber is by raw material point
For natural rubber and synthetic rubber；It is divided into block rubber, latex, liquid rubber and powdered rubber by form.Latex is rubber
Colloidal aqueous dispersion；Liquid rubber is the oligomer of rubber, generally sticky liquid before unvulcanized；Powdered rubber is by breast
Glue be processed into it is powdered, with sharp dispensing and processing and fabricating.
The most common rubber mixing technique flow of modern rubber industry is：Reinforcing agent that rubber is coordinated with it, vulcanizing agent, promotion
Agent, age resistor, softening agent, filler etc. mix kneading into elastomeric compound semi-finished product.Since American inventor Charlie in 1844 is ancient
Since moral Ilyushin has invented vulcanization rubber technology, following substantially technological process has been followed always：Tree cut latex-be dried into dry glue-
It plasticate-is kneaded, the ingredients such as sulphur, reinforcing agent, age resistor, softening agent, filler and accelerator is added during mixing, are finally obtained into
Product, vulcanization are last one of manufacturing procedures therein.Vulcanization be exactly sizing material under certain condition, rubber macromolecule is by linear structure
It is changed into the cross-linking process of network structure.However, there is the problem of three aspects in this traditional handicraft for natural rubber：
(1) product obtained by is unable to reach more than 80% high rebound degree, and shore hardness is higher than 38 degree, tensile strength
Less than 28MPa, therefore, obtained product rebound degree is low, hardness is high, tensile strength is low, and its combination property is not good enough, can not apply
In the very big mine abrasion-proof accessories of discrete element pounding wear；
(2) in mixing process, environment can be caused to a certain degree as the carbon black of reinforcing agent and other powdery dispensings
On pollution, so as to influence the health of operating personnel；
(3) in plasticating and being kneaded this two procedures, the energy consumed is too big.
It is to solve the above problems, external anti-using liquid latex, emulsification white carbon, emulsification sulphur, emulsification promoter, emulsification
The ingredients such as old agent are thoroughly mixed under liquid condition, and the process is referred to as liquid and is kneaded, and formedness is obtained after finally drying
The rubber of energy, and rebound degree reaches 80%, shore hardness is 38 degree, tensile strength 25MPa.
However, as the effect of reinforcing agent to can not show a candle to black wood charcoal black for white carbon.But if add black wood charcoal is black as reinforcing agent
Enter into latex, latex can then be demulsified rapidly solidification, so as to lead to not be further continued for mix；In addition, above-mentioned external use
Technological process in, drying process is to be heated at normal temperatures and pressures using microwave or steam through heat radiation caused by exchanger
Carried out under conditions of 100 DEG C or so, however, 100 DEG C of high temperature plays destruction, and thermal effect to the beneficiating ingredient in latex
Rate is low.
The content of the invention
The process units and its method being kneaded it is an object of the invention to provide a kind of liquid rubber, with prior art phase
Than its energy consumption is small, pollution is small, can make black wood charcoal is black to have good dispersion effect, the rubber produced in liquid latex
With the combination property that high resiliency, soft, high maximum elongation and high tensile etc. are excellent.
To achieve the above object, the process units that this liquid rubber is kneaded, including the Raw material processing being sequentially connected and metering
Device, batch mixing output device and product dehydrate and drying device, described batch mixing output device include spreading extrusion die, mixed
Gel extruder, coagulation glue storage tank and static mixer；The upper end of the static mixer and Raw material processing and metering device phase
Even, its lower end is connected with coagulation glue storage tank；The lower end of the coagulation glue storage tank is connected with coagulation rubber extruding machine；It is described to spread extrusion
The left end of die head is connected with coagulation rubber extruding machine, and its right-hand member is connected with product dehydrate and drying device；Described Raw material processing and
Metering device includes mixed latex liquid constant displacement pump, carbon black emulsion constant displacement pump, carbon black emulsifying mill, carbon black measuring tank, vulcanizing agent breast
Change mill, vulcanizing agent measuring tank, age resistor emulsifying mill, age resistor measuring tank, accelerator emulsifying mill, accelerator measuring tank, antiscorching agent
Emulsifying mill, antiscorching agent measuring tank, latex measuring tank, latex storage tank, emulsion pump, emulsion mixing weighing tank and mixed glue solution
Delivery pump, the carbon black emulsifying mill, vulcanizing agent emulsifying mill, age resistor emulsifying mill, accelerator emulsifying mill and antiscorching agent emulsifying mill
Lower end is upper with carbon black measuring tank, vulcanizing agent measuring tank, age resistor measuring tank, accelerator measuring tank and antiscorching agent measuring tank respectively
End is connected；The lower end of the latex storage tank is connected by emulsion pump with the upper end of latex measuring tank；The carbon black metering
The lower end of tank is connected with carbon black emulsion constant displacement pump；It is the vulcanizing agent measuring tank, age resistor measuring tank, accelerator measuring tank, anti-
Upper end of the lower end of burnt agent measuring tank and latex measuring tank with emulsion mixing weighing tank is connected；The emulsion mixing weighing tank
Lower end is connected by mixed glue solution delivery pump with mixed latex liquid constant displacement pump；The mixed latex liquid constant displacement pump and carbon black emulsion
Constant displacement pump is in parallel with the upper end of static mixer.
Preferably, described static mixer is duct type static mixer.
Preferably, described coagulation rubber extruding machine is one kind in screw, gear type and diaphragm type.
Preferably, described carbon black emulsifying mill, vulcanizing agent emulsifying mill, age resistor emulsifying mill, accelerator emulsifying mill and anti-scorch
Agent emulsifying mill is vacuum basket type sand mill.
Preferably, described emulsion pump is one kind in membrane pump, piston pump and peristaltic pump.
Preferably, described product dehydrate and drying device include elastomeric compound load wagon, elastomeric compound rear pump, microwave drying
Stove, water leg and dewaterer, the water leg are placed on the lower section of dewaterer；The transmission belt of the microwave drying furnace interior is from a left side
To the right side through between dewaterer and elastomeric compound rear pump；The elastomeric compound load wagon is located at the lower section of elastomeric compound rear pump；Institute
State dewaterer and be connected with spreading the right-hand member of extrusion die.
Compared with prior art, the present invention has the advantage that：
(1) mixing suitable for liquid rubber produces and processes, and environment is made so as to avoid carbon black and other powdery dispensings
Into pollution；
(2) when black wood charcoal is black to be added to as reinforcing agent in latex, static mixer of the invention, it can prevent that latex is fast
The problem of speed demulsification solidification, so as to make black wood charcoal is black there is good dispersion effect in liquid latex；
(3) in of the invention product dehydrate and drying device, microwave drier design temperature is less than 70, DEG C and foreign technology
To compare, its drying temperature is low, and so as to prevent destruction of the high temperature to the beneficiating ingredient in latex, and its thermal efficiency is high, so that
It is low to obtain whole process units energy consumption；
(4) rubber that the process units is produced has high resiliency, soft, high maximum elongation and high tensile
Etc. excellent combination property.
Brief description of the drawings
Fig. 1 is the overall schematic of the present invention；
Fig. 2 is the structural representation of Raw material processing and metering device in the present invention；
Fig. 3 is the structural representation of batch mixing output device in the present invention；
Fig. 4 is the structural representation of product dehydrate and drying device in the present invention；
In figure：1st, Raw material processing and metering device, 2, batch mixing output device, 3, dehydration and drying device, 4, mixed latex
Liquid constant displacement pump, 5, carbon black emulsion constant displacement pump, 6, carbon black emulsifying mill, 7, carbon black measuring tank, 8, vulcanizing agent emulsifying mill, 9, vulcanizing agent
Measuring tank, 10, age resistor emulsifying mill, 11, age resistor measuring tank, 12, accelerator emulsifying mill, 13, accelerator measuring tank, 14, anti-
Burnt agent emulsifying mill, 15, antiscorching agent measuring tank, 16, latex measuring tank, 17, latex storage tank, 18, emulsion pump, 19, emulsion
Mixing weighing tank, 20, mixed glue solution delivery pump, 21, elastomeric compound load wagon, 22, elastomeric compound rear pump, 23, microwave drier,
24th, water leg, 25, dewaterer, 26, spread extrusion die, 27, coagulation rubber extruding machine, 28, coagulation glue storage tank, 29, static mixing
Device.
Embodiment
The present invention is described in further detail below in conjunction with accompanying drawing.
As shown in figure 1, this liquid rubber be kneaded process units, including be sequentially connected Raw material processing and metering device 1,
Batch mixing output device 2 and product dehydrate and drying device 3.As shown in figure 3, batch mixing output device 2 includes spreading extrusion die
26th, coagulation rubber extruding machine 27, coagulation glue storage tank 28 and static mixer 29；The upper end of the static mixer 29 and Raw material processing
It is connected with metering device 1, its lower end is connected with coagulation glue storage tank 28；The lower end of the coagulation glue storage tank 28 and coagulation rubber extruding machine
27 are connected；The left end for spreading extrusion die 26 is connected with coagulation rubber extruding machine 27, its right-hand member and product dehydrate and dry dress
3 are put to be connected.
Described static mixer 29 can be duct type static mixer, or SV types static mixer, SK types
Static mixer, SX types static mixer, SH types static mixer and SH type static mixers.What is selected in the present invention is pipe
Road formula static mixer, because duct type static mixer compared with other 5 kinds of static mixers, has more efficient, quick, low
The advantages that energy consumption, good diffusion effect.
Described coagulation rubber extruding machine 27 can be one kind in screw, gear type and diaphragm type.
As shown in Fig. 2 the Raw material processing and metering device 1 in the present invention include mixed latex liquid constant displacement pump 4, carbon black emulsifies
Liquid constant displacement pump 5, carbon black emulsifying mill 6, carbon black measuring tank 7, vulcanizing agent emulsifying mill 8, vulcanizing agent measuring tank 9, age resistor emulsifying mill 10,
Age resistor measuring tank 11, accelerator emulsifying mill 12, accelerator measuring tank 13, antiscorching agent emulsifying mill 14, antiscorching agent measuring tank 15, breast
Glue measuring tank 16, latex storage tank 17, emulsion pump 18, emulsion mixing weighing tank 19 and mixed glue solution delivery pump 20, it is described
Carbon black emulsifying mill 6, vulcanizing agent emulsifying mill 8, age resistor emulsifying mill 10, the lower end of accelerator emulsifying mill 12 and antiscorching agent emulsifying mill 14
Respectively with carbon black measuring tank 7, vulcanizing agent measuring tank 9, age resistor measuring tank 11, accelerator measuring tank 13 and antiscorching agent measuring tank 15
Upper end be connected；The lower end of the latex storage tank 17 is connected by emulsion pump 18 with the upper end of latex measuring tank 16；Institute
The lower end for stating carbon black measuring tank 7 is connected with carbon black emulsion constant displacement pump 5；The vulcanizing agent measuring tank 9, age resistor measuring tank 11,
Upper end phase of the lower end of accelerator measuring tank 13, antiscorching agent measuring tank 15 and latex measuring tank 16 with emulsion mixing weighing tank 19
Even；The lower end of the emulsion mixing weighing tank 19 is connected by mixed glue solution delivery pump 20 with mixed latex liquid constant displacement pump 4；It is described
Mixed latex liquid constant displacement pump 4 and carbon black emulsion constant displacement pump 5 are in parallel with the upper end of static mixer 29.The present invention can also use people
Work is stirred and measured, but it need to consume substantial amounts of people compared with the Raw material processing and metering device 1 that are used in the present embodiment
Power and efficiency is low, can not realize automated production.
Described carbon black emulsifying mill 6, vulcanizing agent emulsifying mill 8, age resistor emulsifying mill 10, accelerator emulsifying mill 12 and antiscorching agent
Emulsifying mill 14 is vacuum basket type sand mill, or horizontal sand mill or vertical grinding machine.What is selected in the present invention is
Vacuum basket type sand mill, because being applied to process units production efficiency height, and Emulsion particle size point from vacuum basket type sand mill
Cloth section is narrower, distribution of particles evenly so that emulsion dispersion is better.
Described emulsion pump 18 is one kind in membrane pump, piston pump and peristaltic pump.
As shown in figure 4, the product dehydrate and drying device 3 in the present invention include elastomeric compound load wagon 21, elastomeric compound exports
Pump 22, microwave drier 23, water leg 24 and dewaterer 25, the water leg 24 are placed on the lower section of dewaterer 25；It is described micro-
Transmission belt inside ripple drying oven 23 is from left to right through between dewaterer 25 and elastomeric compound rear pump 22；The mixing mucilage binding
Carrier vehicle 21 is located at the lower section of elastomeric compound rear pump 22；The dewaterer 25 is connected with spreading the right-hand member of extrusion die 26.The present invention
Hot-air caused by heated-air drying caused by burning diesel oil or Electric heat oven can also be used to dry, what the present embodiment was selected is
Microwave drier, microwave drying furnace temperature are less than 70 DEG C, and its drying temperature is low, so as to be produced to the beneficiating ingredient in latex
Destruction, and the thermal efficiency is high.
The method being specifically kneaded is：By carbon black, dispersant, the metered carbon black emulsifying mill 6 of water, carbon black meter is entered after emulsification
Measuring tank 7 is standby；By vulcanizing agent, suspending agent, the metered vulcanizing agent emulsifying mill 8 of water, it is standby that vulcanizing agent measuring tank 8 is entered after emulsification
With；By age resistor, suspending agent, the metered age resistor emulsifying mill 10 of water, it is standby that age resistor measuring tank 11 is entered after emulsification；It will promote
Enter agent, suspending agent, the metered accelerator emulsifying mill 12 of water, it is standby that accelerator measuring tank 13 is entered after emulsification；By antiscorching agent, hang
Floating agent, the metered antiscorching agent emulsifying mill 14 of water, it is standby that antiscorching agent measuring tank 15 is entered after emulsification；Latex storage tank will be stored in
It is standby that the latex that concentration in 17 is 60% is added to latex measuring tank 16.
Latex is measured by latex measuring tank 16 and enters emulsion mixing weighing tank 19；Then, emulsification vulcanization is measured respectively
Agent, antioxidant emulsion, emulsification antiscorching agent are mixed into emulsion mixing weighing tank 19, then add emulsification promoter to enter emulsion mixing weighing tank
19, stirring at normal temperature is uniform.
The emulsification carbon black in carbon black measuring tank 7 is stored in through carbon black emulsion constant displacement pump 5, is input into by setting pressure, flow velocity
Enter in static mixer 29；The blended He of glue delivery pump 20 of emulsion mixed liquor priority being stored in emulsion mixing weighing tank 19
Mixed latex liquid constant displacement pump 4, it is input into by setting pressure, flow velocity in static mixer 29.
Carbon black liquid and emulsion mixed liquor are emulsified by a certain percentage, with 7m/s flow velocity, at a high speed into static mixer 29, wink
Between disperse, mix, condense into and enter coagulation glue storage tank 28 containing the flowable mixing of rubber of large quantity of moisture, mixing temperature is less than 70
℃。
Coagulation glue by spreading extrusion die 26, is extruded into piece banding coagulation glue by coagulation glue by coagulation rubber extruding machine 27, is squeezed
The coagulation glue of banding in blocks is entered back into after dewaterer 25 extrudes big portion's moisture, is entered in microwave drier 23 and is dried, moisture content contains
Amount is less than 0.5%, the qualified output of product.
The performance of rubber：
| Detection project | Test result | External Linatex companies index |
| Rebound degree/% | 81±1 | 75±1 |
| Hardness (shore A types)/degree | 38±1 | 38±1 |
| Elongation at break/% | 830±20 | 750±20 |
| Tensile strength/MPa | 32±1 | 25±1 |
As can be seen from the above table, the liquid rubber performance that the present invention produces is superior to the index of external Linatex companies, and
And with excellent combination properties such as high resiliency, soft, high maximum elongation and high tensiles.
Claims (6)
1. the process units that a kind of liquid rubber is kneaded, including the Raw material processing and metering device (1), the batch mixing that are sequentially connected export
Device (2) and product dehydrate and drying device (3), it is characterised in that：Described batch mixing output device (2) includes spreading extrusion
Die head (26), coagulation rubber extruding machine (27), coagulation glue storage tank (28) and static mixer (29)；The static mixer (29)
Upper end is connected with Raw material processing and metering device (1), and its lower end is connected with coagulation glue storage tank (28)；The coagulation glue storage tank (28)
Lower end be connected with coagulation rubber extruding machine (27)；The left end for spreading extrusion die (26) and coagulation rubber extruding machine (27) phase
Even, its right-hand member is connected with product dehydrate and drying device (3)；
Described Raw material processing and metering device (1) include mixed latex liquid constant displacement pump (4), carbon black emulsion constant displacement pump (5), charcoal
It is black emulsifying mill (6), carbon black measuring tank (7), vulcanizing agent emulsifying mill (8), vulcanizing agent measuring tank (9), age resistor emulsifying mill (10), anti-
Old agent measuring tank (11), accelerator emulsifying mill (12), accelerator measuring tank (13), antiscorching agent emulsifying mill (14), antiscorching agent metering
Tank (15), latex measuring tank (16), latex storage tank (17), emulsion pump (18), emulsion mixing weighing tank (19) and mixing
Glue delivery pump (20), the carbon black emulsifying mill (6), vulcanizing agent emulsifying mill (8), age resistor emulsifying mill (10), accelerator emulsification
Measured respectively with carbon black measuring tank (7), vulcanizing agent measuring tank (9), age resistor the lower end for grinding (12) and antiscorching agent emulsifying mill (14)
The upper end of tank (11), accelerator measuring tank (13) and antiscorching agent measuring tank (15) is connected；The lower end of the latex storage tank (17)
It is connected by emulsion pump (18) with the upper end of latex measuring tank (16)；The lower end of the carbon black measuring tank (7) and carbon black breast
Change liquid constant displacement pump (5) to be connected；It is the vulcanizing agent measuring tank (9), age resistor measuring tank (11), accelerator measuring tank (13), anti-scorch
Upper end of the lower end of agent measuring tank (15) and latex measuring tank (16) with emulsion mixing weighing tank (19) is connected；The emulsion mixes
The lower end of total measuring tank (19) is connected by mixed glue solution delivery pump (20) with mixed latex liquid constant displacement pump (4)；The mixing breast
Glue constant displacement pump (4) and carbon black emulsion constant displacement pump (5) are in parallel with the upper end of static mixer (29).
2. the process units that a kind of liquid rubber according to claim 1 is kneaded, it is characterised in that：Described static mixing
Device (29) is duct type static mixer.
3. the process units that a kind of liquid rubber according to claim 1 or 2 is kneaded, it is characterised in that：Described coagulation
Rubber extruding machine (27) is one kind in screw, gear type and diaphragm type.
4. the process units that a kind of liquid rubber according to claim 1 is kneaded, it is characterised in that：Described carbon black emulsification
It is true to grind (6), vulcanizing agent emulsifying mill (8), age resistor emulsifying mill (10), accelerator emulsifying mill (12) and antiscorching agent emulsifying mill (14)
Empty basket type sand mill.
5. the process units that a kind of liquid rubber according to claim 1 is kneaded, it is characterised in that：Described latex conveying
Pump (18) is one kind in membrane pump, piston pump and peristaltic pump.
6. the process units that a kind of liquid rubber according to claim 1 or 2 is kneaded, it is characterised in that：Described product
Dehydration and drying device (3) include elastomeric compound load wagon (21), elastomeric compound rear pump (22), microwave drier (23), water leg
(24) and dewaterer (25), the water leg (24) are placed on the lower section of dewaterer (25)；The microwave drier (23) is internal
Transmission belt from left to right through between dewaterer (25) and elastomeric compound rear pump (22)；Elastomeric compound load wagon (21) position
In the lower section of elastomeric compound rear pump (22)；The dewaterer (25) is connected with spreading the right-hand member of extrusion die (26).
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510167656.7A CN104786381B (en) | 2015-04-09 | 2015-04-09 | The process units and its method that a kind of liquid rubber is kneaded |
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|---|---|---|---|
| CN201510167656.7A CN104786381B (en) | 2015-04-09 | 2015-04-09 | The process units and its method that a kind of liquid rubber is kneaded |
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| CN104786381A CN104786381A (en) | 2015-07-22 |
| CN104786381B true CN104786381B (en) | 2018-02-23 |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0064813A2 (en) * | 1981-04-17 | 1982-11-17 | Mobil Oil Corporation | A method of making optically clear oriented polyimide film |
| CN103613919A (en) * | 2013-11-20 | 2014-03-05 | 南京诚盟机械有限公司 | Shoe material hot-melt adhesive sheet and production process and equipment thereof |
| CN104501564A (en) * | 2014-12-24 | 2015-04-08 | 乳山市日晟机械制造有限公司 | Multilevel drying equipment |
| CN204546816U (en) * | 2015-04-09 | 2015-08-12 | 徐州天诺矿山设备有限公司 | The process units that liquid rubber is mixing |
-
2015
- 2015-04-09 CN CN201510167656.7A patent/CN104786381B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0064813A2 (en) * | 1981-04-17 | 1982-11-17 | Mobil Oil Corporation | A method of making optically clear oriented polyimide film |
| CN103613919A (en) * | 2013-11-20 | 2014-03-05 | 南京诚盟机械有限公司 | Shoe material hot-melt adhesive sheet and production process and equipment thereof |
| CN104501564A (en) * | 2014-12-24 | 2015-04-08 | 乳山市日晟机械制造有限公司 | Multilevel drying equipment |
| CN204546816U (en) * | 2015-04-09 | 2015-08-12 | 徐州天诺矿山设备有限公司 | The process units that liquid rubber is mixing |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104786381A (en) | 2015-07-22 |
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