CN203863871U - Full-automatic integral production line for rubber compound of ethylene propylene rubber - Google Patents
Full-automatic integral production line for rubber compound of ethylene propylene rubber Download PDFInfo
- Publication number
- CN203863871U CN203863871U CN201420239366.XU CN201420239366U CN203863871U CN 203863871 U CN203863871 U CN 203863871U CN 201420239366 U CN201420239366 U CN 201420239366U CN 203863871 U CN203863871 U CN 203863871U
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- Prior art keywords
- extruder barrel
- feeder
- weighing
- screw feeder
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- 229920001971 elastomer Polymers 0.000 title claims abstract description 42
- 239000005060 rubber Substances 0.000 title claims abstract description 42
- 150000001875 compounds Chemical class 0.000 title claims abstract description 20
- 238000004519 manufacturing process Methods 0.000 title abstract description 19
- 229920000181 Ethylene propylene rubber Polymers 0.000 title abstract 3
- 238000005303 weighing Methods 0.000 claims abstract description 70
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims abstract description 52
- 230000007246 mechanism Effects 0.000 claims abstract description 34
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 27
- 229910000019 calcium carbonate Inorganic materials 0.000 claims abstract description 26
- 239000004594 Masterbatch (MB) Substances 0.000 claims abstract description 18
- 239000003054 catalyst Substances 0.000 claims abstract description 16
- 239000003963 antioxidant agent Substances 0.000 claims abstract description 14
- 230000003078 antioxidant effect Effects 0.000 claims abstract description 14
- 239000004927 clay Substances 0.000 claims abstract description 14
- 238000001816 cooling Methods 0.000 claims abstract description 13
- 238000012216 screening Methods 0.000 claims abstract description 12
- 239000000843 powder Substances 0.000 claims description 25
- 239000003292 glue Substances 0.000 claims description 17
- 238000010438 heat treatment Methods 0.000 claims description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- 230000008878 coupling Effects 0.000 claims description 9
- 238000010168 coupling process Methods 0.000 claims description 9
- 238000005859 coupling reaction Methods 0.000 claims description 9
- 230000009467 reduction Effects 0.000 claims description 9
- 238000005452 bending Methods 0.000 claims description 4
- 239000000155 melt Substances 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 13
- 238000010092 rubber production Methods 0.000 abstract description 4
- 230000003749 cleanliness Effects 0.000 abstract description 3
- HQQADJVZYDDRJT-UHFFFAOYSA-N ethene;prop-1-ene Chemical group C=C.CC=C HQQADJVZYDDRJT-UHFFFAOYSA-N 0.000 abstract 2
- 238000007789 sealing Methods 0.000 abstract 1
- 239000000463 material Substances 0.000 description 21
- 238000005516 engineering process Methods 0.000 description 9
- 238000006243 chemical reaction Methods 0.000 description 7
- 239000002994 raw material Substances 0.000 description 5
- 230000006872 improvement Effects 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 238000001125 extrusion Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 238000004026 adhesive bonding Methods 0.000 description 2
- 238000004132 cross linking Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000009472 formulation Methods 0.000 description 2
- 238000005469 granulation Methods 0.000 description 2
- 230000003179 granulation Effects 0.000 description 2
- 238000005453 pelletization Methods 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 230000011218 segmentation Effects 0.000 description 1
- 229940032021 tetramune Drugs 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
Classifications
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- 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
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/375—Plasticisers, homogenisers or feeders comprising two or more stages
- B29C48/385—Plasticisers, homogenisers or feeders comprising two or more stages using two or more serially arranged screws in separate barrels
-
- 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
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
- B29C48/04—Particle-shaped
-
- 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
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/92—Measuring, controlling or regulating
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/9258—Velocity
- B29C2948/926—Flow or feed rate
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/92704—Temperature
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92819—Location or phase of control
- B29C2948/92857—Extrusion unit
- B29C2948/92876—Feeding, melting, plasticising or pumping zones, e.g. the melt itself
- B29C2948/92895—Barrel or housing
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
The utility model discloses a full-automatic integral production line for a rubber compound of ethylene propylene rubber. The production line comprises weighing feeders, screw feeders, weighing screw feeders, feeders, a cooling screening mechanism and an extruder, wherein an ethylene propylene masterbatch weighing feeder and an ethylene propylene main rubber weighing feeder are connected with a primary procedure screw feeder; an antioxidant weighing screw feeder and a pottery clay weighing screw feeder are connected with a primary procedure calcium carbonate weighing screw feeder and the primary procedure screw feeder; a secondary procedure calcium carbonate weighing screw feeder is connected with a secondary procedure screw feeder; a first-stage extruder charging barrel is connected with a second-stage extruder charging barrel; the end part of the second-stage extruder charging barrel is connected with an extruder granulating mechanism; a catalyst feeder is connected with the first-stage extruder charging barrel; a vulcanizing agent feeder is connected with the second-stage extruder charging barrel. According to the utility model, the production line can automatically product ethylene propylene rubber continuously in a sealing manner in the field of rubber production, the produced rubber compound is high in cleanliness, and the product quality performance is stable.
Description
Technical field
The utility model relates to elastomeric compound production equipment field, particularly relates to a kind of EP rubbers elastomeric compound fully automatic integral streamline.
background technology
EP rubbers is a kind of organic compound Tetramune, is very important raw material in rubber industry, has multiple good physicochemical property.EP rubbers is widely used in multiple industries such as automobile, building fittings, electrical equipment, electric wire.Mainly as shown in Figure 1, concrete steps are as follows in the production of current second the third mixing of rubber: the weighing operation of 1) first manually getting the raw materials ready; 2) ready material is put into banbury and carry out banburying; 3) material after banburying is put into mill and open refining; 4) through interleaving agent groove; 5) be dried, grind page and process; 6) carry out rolling, weigh.More than be operating as that segmentation carries out, therefore production efficiency is low, and dust pollution is serious, and labor strength is high, and gets the raw materials ready by manually carrying out, and dosage is often also incomplete same, and therefore product quality is often unified not.
Utility model content
For above problem, the utility model provides a kind of EP rubbers elastomeric compound fully automatic integral streamline and processing technology, this production line can be produced EP rubbers automatically in the continuous closure in rubber production field, all production is that mixing 24 hours of continuity is uninterrupted, its all powders, plastochondria is unified dispensing by warehouse pipeline, material leaks without any, therefore the elastomeric compound cleanliness factor of producing is high, product quality stable performance, for reaching this object, the utility model provides a kind of fully automatic integral streamline of EP rubbers elastomeric compound processing technology, comprise weighing charging device, screw feeder, the screw feeder of weighing, feeder, cooling, screening mechanism and extruder, described weighing charging device comprises second the third rubber master batch weighing charging device and the main glue weighing charging of second third device, described second the third rubber master batch weighing charging device is connected with the main glue weighing charging of second third device, described second the third rubber master batch weighing charging device is connected with the charging hopper of the first operation screw feeder by connecting pipe with the main glue weighing charging of second third device, described screw feeder comprises the antioxidant screw feeder of weighing, the potter's clay screw feeder of weighing, the first operation calcium carbonate screw feeder and the second operation calcium carbonate screw feeder of weighing of weighing, the described antioxidant screw feeder of weighing, potter's clay screw feeder and the first operation calcium carbonate screw feeder of weighing of weighing is connected with the charging hopper of the first operation screw feeder by connecting pipe, described the second operation calcium carbonate screw feeder of weighing is connected with the charging hopper of the second operation screw feeder by connecting pipe, described extruder comprises main motor, reduction box, shaft coupling, extruder granulating mechanism, the first rank extruder barrel and second-order extruder barrel, described main motor connects reduction box, described main motor connects the first rank extruder barrel, described second-order extruder barrel is below the first rank extruder barrel, after described the first extruder barrel end, rank bending, connect second-order extruder barrel, in described the first rank extruder barrel and second-order extruder barrel junction, there is Melt Pump, described second-order extruder barrel end connects extruder granulating mechanism, described extruder granulating mechanism is Water ring granulator, in described the first rank extruder barrel, have and in a pair of screw rod and second-order extruder barrel, have a single screw rod, the rotating shaft of described main motor connects the screw rod in the first rank extruder barrel by shaft coupling, described extruder granulating mechanism meets cooling, screening mechanism by pipeline, on described the first rank extruder barrel, there are 3 oil plant entrances, there are 2 powder entrances described the first extruder barrel side, rank, the interface of the screw rod of described the first operation screw feeder connects the powder entrance of the first rank extruder barrel by main motor one side by pipeline, the interface of the screw rod of described the second operation screw feeder connects the powder entrance of the first rank extruder barrel by second-order extruder barrel one side by pipeline, described feeder comprises catalyst feeder and vulcanizing agent feeder, described catalyst feeder is between two powder entrances, described catalyst feeder connects the first rank extruder barrel by pipeline, described vulcanizing agent feeder is between the first rank extruder barrel kink and extruder granulating mechanism, described vulcanizing agent feeder connects second-order extruder barrel by pipeline, described the first rank extruder barrel and second-order extruder barrel are set with heating ring outward, the inwall of described heating ring is fixed with water Xun ring temperature control pipeline.
As further improvement of the utility model, in the Melt Pump in described the first rank extruder barrel and second-order extruder barrel junction, there is filter screen, filter screen is set in Melt Pump, prevent that the large-sized solid that unreacted completes from passing through filter screen.
As further improvement of the utility model, described extruder also comprises apparatus for vacuum producing, described the first rank extruder barrel has apparatus for vacuum producing by second-order extruder barrel one side end top, first stage can vacuumize to remove the space between reacting rear material to reacting rear material by apparatus for vacuum producing after having reacted, and makes reaction more abundant.
As further improvement of the utility model, described the first rank extruder barrel is set with 5-7 joint heating ring outward, needing the utility model first stage is to use heat stepwise, therefore can use more piece heating ring to heat, and concrete joint number can be selected according to actual needs.
As further improvement of the utility model, in described second-order extruder barrel, having a single screw rod is screw pin, has multiple teeth on screw pin, can carry out more sufficiently uniformly mixing after use screw pin.
The utility model provides a kind of EP rubbers elastomeric compound fully automatic integral streamline and processing technology, this production line can be produced EP rubbers automatically in the continuous closure in rubber production field, all production is that mixing 24 hours of continuity is uninterrupted, therefore can realize uninterrupted production, thereby can greatly improve production efficiency, in addition all powders of the utility model, plastochondria is unified dispensing by warehouse pipeline, batching accurately, material leaks without any, and production line can be realized increasingly automated accurate production, all feeding in raw material/conveying is pressed original formulation unified management by middle control CPU, all pipeline material flows are all controlled in +/-0.1% error, therefore the material accuracy coordinating is high, product quality stable performance, in addition the utility model peroxide (vulcanizing agent) adopts injection system to annotate, therefore can greatly improve the quality of products and stability, in addition the utility model adopts single Screw Extrusion pelletizing technique, therefore product is directly granular, and traditional product is film, carry out again needing hand fed in secondary operations, pelletized product is without considering this problem, the utility model is by traditional banburying, open refining, filter, add sulphur, rolling over the process combination such as page becomes through raw material automatic transport, mix to extrude continuously and add single Screw Extrusion pelletizing technique, whole production technology is accomplished without any letup, on-the-spot clean, can significantly reduce labour intensity, realize full-automatic production.
Brief description of the drawings
Fig. 1 is the utility model prior art schematic diagram;
Fig. 2 is the utility model schematic diagram;
Member in figure is:
1-1, second the third rubber master batch weighing charging device; 1-2, the main glue weighing charging of second third device;
2-1, the first operation screw feeder; 2-2, the second operation screw feeder;
3-1, the antioxidant screw feeder of weighing; 3-2, the potter's clay screw feeder of weighing;
3-3, the first operation calcium carbonate screw feeder of weighing;
3-4, the second operation calcium carbonate screw feeder of weighing;
4-1, catalyst feeder; 4-2, vulcanizing agent feeder;
5, cooling, screening mechanism; 6-1, main motor;
6-2, reduction box; 6-3, shaft coupling;
6-4, oil plant entrance; 6-5, powder entrance;
6-6, apparatus for vacuum producing; 6-7, extruder granulating mechanism;
6-8, the first rank extruder barrel; 6-9, second-order extruder barrel.
Detailed description of the invention
Below in conjunction with drawings and Examples, utility model is described in detail:
The utility model provides a kind of EP rubbers elastomeric compound fully automatic integral streamline and processing technology, this production line can be produced EP rubbers automatically in the continuous closure in rubber production field, all production is that mixing 24 hours of continuity is uninterrupted, its all powders, plastochondria is unified dispensing by warehouse pipeline, material leaks without any, and the elastomeric compound cleanliness factor of therefore producing is high, product quality stable performance.
The processing technology of a kind of EP rubbers elastomeric compound of the utility model, described processes step is as follows:
1) by second the third rubber master batch weighing charging device 1-1 and the main glue weighing charging of second third device 1-2, required second the third rubber master batch and the main glue of second third are weighed;
2) by antioxidant screw feeder 3-1, potter's clay screw feeder 3-2, the first operation calcium carbonate screw feeder 3-3 that weighs that weighs that weighs, antioxidant, potter's clay and the required calcium carbonate of the first operation are weighed;
3) weighed second the third rubber master batch and the main glue of second third enters the charging hopper of the first operation screw feeder 2-1 by pipeline, and antioxidant, potter's clay and the required calcium carbonate of the first operation enter pipeline and enter the charging hopper of the first operation screw feeder 2-1 by the weigh screw rod transmission of screw feeder of correspondence after having weighed;
4) the first operation screw feeder 2-1 is by second the third rubber master batch and the main glue of second third and antioxidant, after mixing, potter's clay and the required calcium carbonate of the first operation sends into the powder entrance 6-5 of the first rank extruder barrel 6-8 by main motor 6-1 mono-side by screw rod, each oil plant analog assistant injects the oil plant entrance 6-4 of the first rank extruder barrel 6-8 by measuring pump simultaneously, catalyst except vulcanizing agent adds the first rank extruder barrel 6-8 by catalyst feeder 4-1, powder vulcanizing agent is inputted by 3 ~ 3.5Phr, often excess Temperature of closure continuously, if and just reaction just adds vulcanizing agent, because excess Temperature material can occur gluing, after the utility model cooling, add again vulcanizing agent just can avoid material to occur so gluing, input by 3 ~ 3.5Phr in order to ensure product temperature powder vulcanizing agent,
5) the first rank extruder barrel 6-8 is weighed to required calcium carbonate by the second operation calcium carbonate screw feeder 3-4 that weighs after having reacted in advance, after weighing, send into the powder entrance 6-5 of the first rank extruder barrel 6-8 by second-order extruder barrel 6-9 mono-side by the second operation screw feeder 2-2 by screw rod, whole technique heats through different heating ring successively in the first rank extruder barrel 6-8, reaction temperature is 120 degrees Celsius, 130 degrees Celsius, 140 degrees Celsius, 150 degrees Celsius, 160 degrees Celsius, carry out temperature control by extrusion screw rod and barrel by water Xun ring temperature control pipeline, after completing, heat stepwise by apparatus for vacuum producing, reacting rear material is vacuumized, after completing, the utility model heat stepwise can vacuumize to remove by apparatus for vacuum producing the air void of mixing rear storeroom to reacting rear material, material is mixed more abundant, after question response completes, temperature is down to 120 degrees Celsius and is entered second-order extruder barrel 6-9 after following,
6) material enters after second-order extruder barrel 6-9 that to carry out vulcanizing agent by vulcanizing agent feeder 4-2 reinforced, second-order extruder is equipped with dowel special screw rod, Water ring granulator granulation in extruder granulating mechanism 6-7 again after utilizing screw rod mixing sufficiently uniformly, wherein powder vulcanizing agent is inputted by 3 ~ 3.5Phr, produce and add often excess Temperature continuously, if and just add vulcanizing agent in the first rank extruder mix stage, because cross-linking reaction can occur excess Temperature material, the utility model adds vulcanizing agent just can avoid like this material generation cross-linking reaction after heat sink is set again.In order to ensure vulcanizing agent input evenly, adopt screw rod metering input unit, guarantee input precision and uniformity;
7) granulation is carried out cooling, screening processing through cooling, screening mechanism 5 after completing.
More than all pipeline material of technique flow described in reaction is all controlled in +/-0.1% error, due to the utility model be fully automatic integral streamline therefore reinforced/carry by middle control CPU by original formulation unified management, can on demand all pipeline material flows be all controlled at +/-0.1% error with interior to obtain the product of best in quality.
As a kind of specific embodiment of the utility model, the fully automatic integral streamline of a kind of EP rubbers elastomeric compound of the utility model processing technology, comprise weighing charging device, screw feeder, the screw feeder of weighing, feeder, cooling, screening mechanism 5 and extruder, described weighing charging device comprises second the third rubber master batch weighing charging device 1-1 and the main glue weighing charging of second third device 1-2, described second the third rubber master batch weighing charging device 1-1 is connected with the main glue weighing charging of second third device 1-2, described second the third rubber master batch weighing charging device 1-1 is connected with the charging hopper of the first operation screw feeder 2-1 by connecting pipe with the main glue weighing charging of second third device 1-2, described screw feeder comprises the antioxidant screw feeder 3-1 that weighs, the potter's clay screw feeder 3-2 that weighs, the first operation calcium carbonate screw feeder 3-3 and the second operation calcium carbonate screw feeder 3-4 that weighs that weighs, the described antioxidant screw feeder 3-1 that weighs, potter's clay screw feeder 3-2 and the first operation calcium carbonate screw feeder 3-3 that weighs that weighs is connected with the charging hopper of the first operation screw feeder 2-1 by connecting pipe, described the second operation calcium carbonate screw feeder 3-4 that weighs is connected with the charging hopper of the second operation screw feeder 2-2 by connecting pipe, described extruder comprises main motor 6-1, reduction box 6-2, shaft coupling 6-3, extruder granulating mechanism 6-7, the first rank extruder barrel 6-8 and second-order extruder barrel 6-9, described main motor 6-1 meets reduction box 6-2, described main motor 6-1 meets the first rank extruder barrel 6-8, described second-order extruder barrel 6-9 is below the first rank extruder barrel 6-8, after described the first extruder barrel 6-8 end, rank bending, meet second-order extruder barrel 6-9, in described the first rank extruder barrel 6-8 and second-order extruder barrel 6-9 junction, there is Melt Pump, described second-order extruder barrel 6-9 end meets extruder granulating mechanism 6-7, described extruder granulating mechanism 6-7 is Water ring granulator, in described the first rank extruder barrel 6-8, have in a pair of screw rod and second-order extruder barrel 6-9 and have a single screw rod, the rotating shaft of described main motor 6-1 connects the screw rod in the first rank extruder barrel 6-8 by shaft coupling 6-3, described extruder granulating mechanism 6-7 meets cooling, screening mechanism 5 by pipeline, on described the first rank extruder barrel 6-8, there are 3 oil plant entrance 6-4, there are 2 powder entrance 6-5 described the first extruder barrel 6-8 side, rank, the interface of the screw rod of described the first operation screw feeder 2-1 meets the powder entrance 6-5 of the first rank extruder barrel 6-8 by main motor 6-1 mono-side by pipeline, the interface of the screw rod of described the second operation screw feeder 2-2 meets the powder entrance 6-5 of the first rank extruder barrel 6-8 by second-order extruder barrel 6-9 mono-side by pipeline, described feeder comprises catalyst feeder 4-1 and vulcanizing agent feeder 4-2, described catalyst feeder 4-1 is between two powder entrance 6-5, described catalyst feeder 4-1 meets the first rank extruder barrel 6-8 by pipeline, described vulcanizing agent feeder 4-2 is between the first rank extruder barrel 6-8 kink and extruder granulating mechanism 6-7, described vulcanizing agent feeder 4-2 meets second-order extruder barrel 6-9 by pipeline, described the first rank extruder barrel 6-8 and second-order extruder barrel 6-9 are set with heating ring outward, the inwall of described heating ring is fixed with water Xun ring temperature control pipeline.
As a kind of best specific embodiment of the utility model, the utility model provides the fully automatic integral streamline of a kind of EP rubbers elastomeric compound processing technology as shown in Figure 1, comprise weighing charging device, screw feeder, the screw feeder of weighing, feeder, cooling, screening mechanism 5 and extruder, described weighing charging device comprises second the third rubber master batch weighing charging device 1-1 and the main glue weighing charging of second third device 1-2, described second the third rubber master batch weighing charging device 1-1 is connected with the main glue weighing charging of second third device 1-2, described second the third rubber master batch weighing charging device 1-1 is connected with the charging hopper of the first operation screw feeder 2-1 by connecting pipe with the main glue weighing charging of second third device 1-2, described screw feeder comprises the antioxidant screw feeder 3-1 that weighs, the potter's clay screw feeder 3-2 that weighs, the first operation calcium carbonate screw feeder 3-3 and the second operation calcium carbonate screw feeder 3-4 that weighs that weighs, the described antioxidant screw feeder 3-1 that weighs, potter's clay screw feeder 3-2 and the first operation calcium carbonate screw feeder 3-3 that weighs that weighs is connected with the charging hopper of the first operation screw feeder 2-1 by connecting pipe, described the second operation calcium carbonate screw feeder 3-4 that weighs is connected with the charging hopper of the second operation screw feeder 2-2 by connecting pipe, described extruder comprises main motor 6-1, reduction box 6-2, shaft coupling 6-3, extruder granulating mechanism 6-7, the first rank extruder barrel 6-8 and second-order extruder barrel 6-9, described main motor 6-1 meets reduction box 6-2, described main motor 6-1 meets the first rank extruder barrel 6-8, described second-order extruder barrel 6-9 is below the first rank extruder barrel 6-8, after described the first extruder barrel 6-8 end, rank bending, meet second-order extruder barrel 6-9, in described the first rank extruder barrel 6-8 and second-order extruder barrel 6-9 junction, there is Melt Pump, in Melt Pump in described the first rank extruder barrel 6-8 and second-order extruder barrel 6-9 junction, there is filter screen, filter screen is set in Melt Pump, prevent that the large-sized solid that unreacted completes from passing through filter screen, described second-order extruder barrel 6-9 end meets extruder granulating mechanism 6-7, described extruder granulating mechanism 6-7 is Water ring granulator, in described the first rank extruder barrel 6-8, have in a pair of screw rod and second-order extruder barrel 6-9 and have a single screw rod, in described second-order extruder barrel 6-9, having a single screw rod is screw pin, on screw pin, there are multiple teeth, after use screw pin, can carry out more sufficiently uniformly mixing, the rotating shaft of described main motor 6-1 connects the screw rod in the first rank extruder barrel 6-8 by shaft coupling 6-3, described extruder granulating mechanism 6-7 meets cooling, screening mechanism 5 by pipeline, on described the first rank extruder barrel 6-8, there are 3 oil plant entrance 6-4, there are 2 powder entrance 6-5 described the first extruder barrel 6-8 side, rank, the interface of the screw rod of described the first operation screw feeder 2-1 meets the powder entrance 6-5 of the first rank extruder barrel 6-8 by main motor 6-1 mono-side by pipeline, the interface of the screw rod of described the second operation screw feeder 2-2 meets the powder entrance 6-5 of the first rank extruder barrel 6-8 by second-order extruder barrel 6-9 mono-side by pipeline, described feeder comprises catalyst feeder 4-1 and vulcanizing agent feeder 4-2, described catalyst feeder 4-1 is between two powder entrance 6-5, described catalyst feeder 4-1 meets the first rank extruder barrel 6-8 by pipeline, described vulcanizing agent feeder 4-2 is between the first rank extruder barrel 6-8 kink and extruder granulating mechanism 6-7, described vulcanizing agent feeder 4-2 meets second-order extruder barrel 6-9 by pipeline, described the first rank extruder barrel 6-8 and second-order extruder barrel 6-9 are set with heating ring outward, described the first rank extruder barrel 6-8 is set with 5-7 joint heating ring outward, needing the utility model first stage is to use heat stepwise, therefore can use more piece heating ring to heat, concrete joint number can be selected according to actual needs, the inwall of described heating ring is fixed with water Xun ring temperature control pipeline, described extruder also comprises apparatus for vacuum producing 6-6, described the first rank extruder barrel 6-8 has apparatus for vacuum producing 6-6 by second-order extruder barrel 6-9 mono-side end top, first stage can vacuumize to remove the space between reacting rear material to reacting rear material by apparatus for vacuum producing after having reacted, make reaction more abundant.
Can obtain the quality product of following performance through above technique, and product compliance rate reaches 97-98% after tested.
The above; it is only preferred embodiment of the present utility model; be not the restriction of the utility model being made to any other form, and according to any amendment or equivalent variations that technical spirit of the present utility model is done, still belong to the utility model scope required for protection.
Claims (5)
1. an EP rubbers elastomeric compound fully automatic integral streamline, comprise weighing charging device, screw feeder, the screw feeder of weighing, feeder, cooling, screening mechanism (5) and extruder, it is characterized in that: described weighing charging device comprises second the third rubber master batch weighing charging device (1-1) and the main glue weighing charging of second third device (1-2), described second the third rubber master batch weighing charging device (1-1) is connected with the main glue weighing charging of second third device (1-2), described second the third rubber master batch weighing charging device (1-1) is connected with the charging hopper of the first operation screw feeder (2-1) by connecting pipe with the main glue weighing charging of second third device (1-2), described screw feeder comprises the antioxidant screw feeder (3-1) of weighing, the potter's clay screw feeder (3-2) of weighing, the first operation calcium carbonate screw feeder (3-3) and the second operation calcium carbonate screw feeder (3-4) of weighing of weighing, the described antioxidant screw feeder (3-1) of weighing, potter's clay screw feeder (3-2) and the first operation calcium carbonate screw feeder (3-3) of weighing of weighing is connected with the charging hopper of the first operation screw feeder (2-1) by connecting pipe, described the second operation calcium carbonate screw feeder (3-4) of weighing is connected with the charging hopper of the second operation screw feeder (2-2) by connecting pipe, described extruder comprises main motor (6-1), reduction box (6-2), shaft coupling (6-3), extruder granulating mechanism (6-7), the first rank extruder barrel (6-8) and second-order extruder barrel (6-9), described main motor (6-1) connects reduction box (6-2), described main motor (6-1) connects the first rank extruder barrel (6-8), described second-order extruder barrel (6-9) is in the first rank extruder barrel (6-8) below, after described the first rank extruder barrel (6-8) end bending, connect second-order extruder barrel (6-9), in described the first rank extruder barrel (6-8) and second-order extruder barrel (6-9) junction, there is Melt Pump, described second-order extruder barrel (6-9) end connects extruder granulating mechanism (6-7), described extruder granulating mechanism (6-7) is Water ring granulator, in described the first rank extruder barrel (6-8), have in a pair of screw rod and second-order extruder barrel (6-9) and have a single screw rod, the rotating shaft of described main motor (6-1) connects the screw rod in the first rank extruder barrel (6-8) by shaft coupling (6-3), described extruder granulating mechanism (6-7) meets cooling, screening mechanism (5) by pipeline, on described the first rank extruder barrel (6-8), there are 3 oil plant entrances (6-4), there are 2 powder entrances (6-5) described the first rank extruder barrel (6-8) side, the interface of the screw rod of described the first operation screw feeder (2-1) connects the powder entrance (6-5) of the first rank extruder barrel (6-8) by main motor (6-1) side by pipeline, the interface of the screw rod of described the second operation screw feeder (2-2) connects the powder entrance (6-5) of the first rank extruder barrel (6-8) by second-order extruder barrel (6-9) side by pipeline, described feeder comprises catalyst feeder (4-1) and vulcanizing agent feeder (4-2), described catalyst feeder (4-1) is between two powder entrances (6-5), described catalyst feeder (4-1) connects the first rank extruder barrel (6-8) by pipeline, described vulcanizing agent feeder (4-2) is between the first rank extruder barrel (6-8) kink and extruder granulating mechanism (6-7), described vulcanizing agent feeder (4-2) connects second-order extruder barrel (6-9) by pipeline, the outer heating ring that is set with of described the first rank extruder barrel (6-8) and second-order extruder barrel (6-9), the inwall of described heating ring is fixed with water Xun ring temperature control pipeline.
2. a kind of EP rubbers elastomeric compound fully automatic integral streamline according to claim 1, is characterized in that: in the Melt Pump in described the first rank extruder barrel (6-8) and second-order extruder barrel (6-9) junction, have filter screen.
3. a kind of EP rubbers elastomeric compound fully automatic integral streamline according to claim 1, it is characterized in that: described extruder also comprises apparatus for vacuum producing (6-6), described the first rank extruder barrel (6-8) has apparatus for vacuum producing (6-6) by second-order extruder barrel (6-9) side end top.
4. a kind of EP rubbers elastomeric compound fully automatic integral streamline according to claim 1, is characterized in that: the outer 5-7 joint heating ring that is set with of described the first rank extruder barrel (6-8).
5. a kind of EP rubbers elastomeric compound fully automatic integral streamline according to claim 1, is characterized in that: in described second-order extruder barrel (6-9), having a single screw rod is screw pin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420239366.XU CN203863871U (en) | 2014-05-12 | 2014-05-12 | Full-automatic integral production line for rubber compound of ethylene propylene rubber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420239366.XU CN203863871U (en) | 2014-05-12 | 2014-05-12 | Full-automatic integral production line for rubber compound of ethylene propylene rubber |
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| Publication Number | Publication Date |
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| CN203863871U true CN203863871U (en) | 2014-10-08 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420239366.XU Withdrawn - After Issue CN203863871U (en) | 2014-05-12 | 2014-05-12 | Full-automatic integral production line for rubber compound of ethylene propylene rubber |
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| CN (1) | CN203863871U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103978582A (en) * | 2014-05-12 | 2014-08-13 | 扬州华声电子实业有限公司 | Ethylene propylene rubber compound rubber automatic integrated streamline and processing technology |
| CN105599268A (en) * | 2016-04-08 | 2016-05-25 | 山东威普斯橡胶股份有限公司 | Production line for producing heat-resisting styrene-butadiene rubber tapes |
| CN106346736A (en) * | 2016-10-13 | 2017-01-25 | 重庆福信强橡塑制品有限公司 | Vehicle window glass sealing rubber strip production line with automatic rolling function |
| CN117946527A (en) * | 2024-03-22 | 2024-04-30 | 成都力多美科技有限公司 | Semi-cured solid self-curing silicone rubber sheet and preparation method thereof |
-
2014
- 2014-05-12 CN CN201420239366.XU patent/CN203863871U/en not_active Withdrawn - After Issue
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103978582A (en) * | 2014-05-12 | 2014-08-13 | 扬州华声电子实业有限公司 | Ethylene propylene rubber compound rubber automatic integrated streamline and processing technology |
| CN103978582B (en) * | 2014-05-12 | 2016-08-24 | 扬州华声电子实业有限公司 | A kind of EP rubbers elastomeric compound fully automatic integral streamline and processing technique |
| CN105599268A (en) * | 2016-04-08 | 2016-05-25 | 山东威普斯橡胶股份有限公司 | Production line for producing heat-resisting styrene-butadiene rubber tapes |
| CN105599268B (en) * | 2016-04-08 | 2017-07-11 | 山东威普斯橡胶股份有限公司 | A kind of streamline for producing heat resistant type butadiene-styrene rubber band |
| CN106346736A (en) * | 2016-10-13 | 2017-01-25 | 重庆福信强橡塑制品有限公司 | Vehicle window glass sealing rubber strip production line with automatic rolling function |
| CN106346736B (en) * | 2016-10-13 | 2018-05-04 | 重庆福信强橡塑制品有限公司 | Glass for vehicle window sealing rubber strip production line with automatic winding function |
| CN117946527A (en) * | 2024-03-22 | 2024-04-30 | 成都力多美科技有限公司 | Semi-cured solid self-curing silicone rubber sheet and preparation method thereof |
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