CN205003568U - Smelt eventually and glue mixing temperature control system - Google Patents
Smelt eventually and glue mixing temperature control system Download PDFInfo
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- CN205003568U CN205003568U CN201520721080.XU CN201520721080U CN205003568U CN 205003568 U CN205003568 U CN 205003568U CN 201520721080 U CN201520721080 U CN 201520721080U CN 205003568 U CN205003568 U CN 205003568U
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- banbury mixer
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- electric heater
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Abstract
The utility model discloses a smelt eventually and glue mixing temperature control system, including banbury mixer, heat exchanger, electric heater and thermoregulation mechanism, the play water end (W. E. ) of heat exchanger is connected through pipeline and electric heater's the end of intaking, electric heater's play water end (W. E. ) divides two the tunnel, and intake end and thermoregulation mechanism through pipeline and banbury mixer are connected respectively, the play water end (W. E. ) of banbury mixer is connected through the pipeline and the end of intaking of thermoregulation mechanism and heat exchanger. This smelt eventually and glue mixing temperature control system can be stable 25 2 DEG C with smelting gluey ambient temperature to the messenger smelts gluey steady quality, and does not basically need the external world to provide internal recycling water, is favorable to the water economy resource, and simultaneously inside refrigeration cycle temperature is suitable, can protect the inside metallic structure of banbury mixer, reduces the great harm that leads to the fact for the system of temperature difference change, also helps the further stability volume of smelting the gum.
Description
Technical field
The utility model relates to refining glue technical field, the particularly mixing temperature control system of a kind of finished composition.
Background technology
Masterbatch adds the residue compounding ingredient in formula through repeatedly mixing continuation, and the sizing material that can enter next procedure obtained, generally obtains final finished composition through two sections or three-stage mixing, and it is significant to refine the quality of glue variation of ambient temperature to sizing material.
At present, the equipment such as Banbury mixer locular wall, rotor, Dump gate generally carry out control temperature by extraneous recirculated water, and the temperature of recirculated water can higher than 35 DEG C in summer, winter can lower than 10 DEG C, because extraneous circulating water temperature is uncontrollable, thus cause refining glue environment temperature to be also difficult to control in rational scope, cause rubber compounding effect unstable; And extraneous recirculated water is unprocessed, by water route systemic circulation in factory, flow directly into and flow out the equipment such as Banbury mixer locular wall, rotor, Dump gate, very easily causing cooling chamber internal incrustation, have a strong impact on heat-transfer effect; In addition, extraneous recirculated water directly flows out, and between glue refining vehicle, discharge supply is large, and recirculated water is crossed cold or overheated, easily the metal surface of infringement Banbury mixer inside.
Utility model content
For solving the problem that extraneous water temperature in existing finished composition process is uncontrollable, affect compound quality and infringement rubber preparing device, the utility model discloses the mixing temperature control system of a kind of finished composition, comprise Banbury mixer, heat interchanger, electric heater and thermoregulation mechanism, the water side of described heat interchanger is connected with the water inlet end of electric heater by pipeline, the water side of described electric heater divides the water inlet end of two-way respectively by pipeline and Banbury mixer and thermoregulation mechanism to be connected, and the water side of described Banbury mixer is connected by the water inlet end of pipeline with thermoregulation mechanism and heat interchanger.
As further improvement of the utility model, described thermoregulation mechanism comprises the variable valve, electropneumatic transducer and the temperature measuring gauge that are connected by pipeline successively, and described variable valve, electropneumatic transducer and temperature measuring gauge are connected by pipeline successively.
As further improvement of the utility model, described variable valve is connected on the pipeline between electric heater and Banbury mixer water inlet end, described electropneumatic transducer is connected with the water side of electric heater by pipeline, and described temperature measuring gauge is connected on the pipeline between Banbury mixer water side and heat interchanger water inlet end.
As further improvement of the utility model, described heat interchanger is plate type heat exchanger, comprises outer loop water route and inner loop water route, and described outer loop water route is provided with water intaking valve and outlet valve, and described inner loop water route is provided with water compensating valve.
As further improvement of the utility model, described Banbury mixer is provided with Banbury mixer cooling sandwith layer and rotor cooling sandwith layer, and described Banbury mixer cooling sandwith layer and rotor cooling sandwith layer are connected by the water inlet end of pipeline and heat interchanger and water side.
The beneficial effects of the utility model are:
The mixing temperature control system of this finished composition can by refining glue ambient temperature-stable at 25 ± 2 DEG C; thus compound quality is stablized; and substantially do not need the external world to provide inner loop water; be conducive to saving water resource; internal cooling circulating water temperature is suitable for simultaneously; the metal construction of Banbury mixer inside can be protected, reduce the larger infringement caused to system of difference variation, also contribute to stablizing compound quality further.
Accompanying drawing explanation
In order to be illustrated more clearly in the technical scheme in the utility model embodiment, be briefly described to the accompanying drawing used required in embodiment below, apparently, accompanying drawing in the following describes is only embodiments more of the present utility model, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Fig. 1 is structural principle schematic diagram of the present utility model, and in figure, arrow represents the flow direction of recirculated water.
Mark in figure: 1-Banbury mixer; 11-Banbury mixer cooling sandwith layer; 12-rotor cooling sandwith layer; 2-heat interchanger; 3-electric heater; 4-thermoregulation mechanism; 41-variable valve; 42-electropneumatic transducer; 43-temperature measuring gauge.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, be clearly and completely described the technical scheme in the utility model embodiment, obviously, described embodiment is only the utility model part embodiment, instead of whole embodiments.
As shown in Figure 1, the mixing temperature control system of a kind of finished composition, comprises Banbury mixer 1, heat interchanger 2, electric heater 3 and thermoregulation mechanism 4; Banbury mixer 1 is provided with Banbury mixer cooling sandwith layer 11 and rotor cooling sandwith layer 12; Heat interchanger 2 is plate type heat exchanger, comprises outer loop water route and inner loop water route, and outer loop water route is provided with water intaking valve 21 and outlet valve 22, and inner loop water route is provided with water compensating valve 23; Thermoregulation mechanism 4 comprises the variable valve 41, electropneumatic transducer 42 and the temperature measuring gauge 43 that are connected by pipeline successively.
The water side of heat interchanger 2 is connected by the water inlet end of pipeline with electric heater 3, lead up to pipeline and be connected through the Banbury mixer cooling sandwith layer 11 of variable valve 41 and Banbury mixer 1 water inlet end and rotor cooling sandwith layer 12 in the water side of electric heater 3, pipeline of separately leading up to is connected with electropneumatic transducer 42.
The Banbury mixer cooling sandwith layer 11 of Banbury mixer 1 water side is connected by the water inlet end of pipeline with heat interchanger 2 with rotor cooling sandwith layer 12, and temperature measuring gauge 43 is connected on the pipeline between Banbury mixer 1 water side and heat interchanger 2 water inlet end.
Banbury mixer 1, heat interchanger 2, between electric heater 3 and thermoregulation mechanism 4, form circulation waterway, one road chilled water enters the inner loop water route of heat interchanger 2 through water compensating valve 23, flow through Banbury mixer cooling sandwith layer 11 and the rotor cooling sandwith layer 12 of water side-electric heater 3-variable valve 41/ electropneumatic transducer 42-Banbury mixer 1 water inlet end of heat interchanger 2 successively, flow through temperature measuring gauge 43 again after absorbing the heat of Banbury mixer 1 and water inlet end through heat interchanger 2 enters inner loop water route; Another road chilled water enters the outer loop water route of heat interchanger 2 through water intaking valve 21, through outlet valve 22 discharges after carrying out heat interchange with inner loop water route; Water compensating valve 23 also has a vital role to be that internally circulation waterway supplements the moisture because evaporating by heat.
When Banbury mixer 1 starts to produce, because working temperature is lower, also need to carry out preheating to the water in the system of entering; After Banbury mixer 1 is produced, internal sizes is mixing starts heat radiation, temperature measuring gauge 43 monitors the technological temperature (being generally 20 DEG C) that system reaches predetermined, is disconnected by the power supply of electric heater 3 by electropneumatic transducer 42, and now electric heater 3 stops heating.
By the temperature monitoring of temperature measuring gauge 43, the temperature height of system can be judged, when system temperature is too high, increase inflow, to reduce system temperature by electropneumatic transducer 42 regulating and controlling valve 41; When system temperature is too low, reduce inflow, to improve system temperature by electropneumatic transducer 42 regulating and controlling valve 41; Reach the object of control system temperature by the way.
Under case of emergency, when the water temperature of internal system chilled water exceeds preset range, the hydro-thermal amount of inner loop is discharged in time, to keep water temperature normal by regulating the outer loop discharge of heat interchanger 2.
The mixing temperature control system of this finished composition can by refining glue ambient temperature-stable at 25 ± 2 DEG C; thus compound quality is stablized; and substantially do not need the external world to provide inner loop water; be conducive to saving water resource; internal cooling circulating water temperature is suitable for simultaneously; the metal construction of Banbury mixer inside can be protected, reduce the larger infringement caused to system of difference variation, also contribute to stablizing compound quality further.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (5)
1. the mixing temperature control system of finished composition, it is characterized in that, comprise Banbury mixer, heat interchanger, electric heater and thermoregulation mechanism, the water side of described heat interchanger is connected by the water inlet end of pipeline with described electric heater, the water side of described electric heater divides the water inlet end of two-way respectively by pipeline and described Banbury mixer and described thermoregulation mechanism to be connected, and the water side of described Banbury mixer is connected by the water inlet end of pipeline with described thermoregulation mechanism and described heat interchanger.
2. the mixing temperature control system of finished composition according to claim 1, is characterized in that, described thermoregulation mechanism comprises variable valve, electropneumatic transducer and temperature measuring gauge, and described variable valve, electropneumatic transducer and temperature measuring gauge are connected by pipeline successively.
3. the mixing temperature control system of finished composition according to claim 2, it is characterized in that, described variable valve is connected on the pipeline between described electric heater and described Banbury mixer water inlet end, described electropneumatic transducer is connected by the water side of pipeline with described electric heater, and described temperature measuring gauge is connected on the pipeline between described Banbury mixer water side and described heat interchanger water inlet end.
4. the mixing temperature control system of finished composition according to claim 3, it is characterized in that, described heat interchanger is plate type heat exchanger, comprises outer loop water route and inner loop water route, described outer loop water route is provided with water intaking valve and outlet valve, and described inner loop water route is provided with water compensating valve.
5. the mixing temperature control system of finished composition according to claim 4, it is characterized in that, described Banbury mixer is provided with Banbury mixer cooling sandwith layer and rotor cooling sandwith layer, and described Banbury mixer cooling sandwith layer and described rotor cooling sandwith layer are connected by the water inlet end of pipeline and described heat interchanger and water side.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520721080.XU CN205003568U (en) | 2015-09-17 | 2015-09-17 | Smelt eventually and glue mixing temperature control system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520721080.XU CN205003568U (en) | 2015-09-17 | 2015-09-17 | Smelt eventually and glue mixing temperature control system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205003568U true CN205003568U (en) | 2016-01-27 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520721080.XU Active CN205003568U (en) | 2015-09-17 | 2015-09-17 | Smelt eventually and glue mixing temperature control system |
Country Status (1)
| Country | Link |
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| CN (1) | CN205003568U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105666725A (en) * | 2016-04-08 | 2016-06-15 | 昆山安泰美科金属材料有限公司 | Internal mixer with temperature control function |
| CN109227996A (en) * | 2018-09-07 | 2019-01-18 | 鞍山彩盛机械制造有限公司 | Rubber internal mixer cooling water flow ratio temperature control device and its control method |
-
2015
- 2015-09-17 CN CN201520721080.XU patent/CN205003568U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105666725A (en) * | 2016-04-08 | 2016-06-15 | 昆山安泰美科金属材料有限公司 | Internal mixer with temperature control function |
| CN109227996A (en) * | 2018-09-07 | 2019-01-18 | 鞍山彩盛机械制造有限公司 | Rubber internal mixer cooling water flow ratio temperature control device and its control method |
| CN109227996B (en) * | 2018-09-07 | 2023-11-21 | 鞍山彩盛机械制造有限公司 | Cooling water flow rate proportion temperature control device of rubber internal mixer and control method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210831 Address after: 262500 No. 7777, Linglongshan North Road, Qingzhou Economic Development Zone, Weifang City, Shandong Province Patentee after: Pilot tire (Qingzhou) Co.,Ltd. Address before: 262500 east of Linglongshan Road north of the high-speed railway line in Qingzhou Economic Development Zone, Weifang City, Shandong Province Patentee before: SHANDONG SHENG SHI TAI LAI RUBBER TECHNOLOGY Co.,Ltd. |
|
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 262500 No. 7777, Linglongshan North Road, Qingzhou Economic Development Zone, Weifang City, Shandong Province Patentee after: Xiongying tire (Qingzhou) Co.,Ltd. Address before: 262500 No. 7777, Linglongshan North Road, Qingzhou Economic Development Zone, Weifang City, Shandong Province Patentee before: Pilot tire (Qingzhou) Co.,Ltd. |