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CN206561617U - A kind of production of resins cooling system - Google Patents

A kind of production of resins cooling system Download PDF

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Publication number
CN206561617U
CN206561617U CN201720030513.6U CN201720030513U CN206561617U CN 206561617 U CN206561617 U CN 206561617U CN 201720030513 U CN201720030513 U CN 201720030513U CN 206561617 U CN206561617 U CN 206561617U
Authority
CN
China
Prior art keywords
heat exchanger
exchanger tube
storage tank
cooling system
oil
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201720030513.6U
Other languages
Chinese (zh)
Inventor
杨宗全
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chongqing Fang Fang New Material Co Ltd
Original Assignee
Chongqing Fang Fang New Material Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Chongqing Fang Fang New Material Co Ltd filed Critical Chongqing Fang Fang New Material Co Ltd
Priority to CN201720030513.6U priority Critical patent/CN206561617U/en
Application granted granted Critical
Publication of CN206561617U publication Critical patent/CN206561617U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model is related to a kind of production of resins cooling system.The production of resins cooling system that the utility model is provided includes retort and cooling system, and cooling system includes sharing heat exchanger tube, and shared heat exchanger tube is arranged in the interlayer of retort;Cold oil storage tank is connected with the first end of shared heat exchanger tube bottom by oil inlet pipe, and deep fat storage tank is connected with the second end at the top of shared heat exchanger tube by flowline;Cold water storage tank is connected with the first end of heat exchanger tube by water inlet pipe, and hot water storage tank is connected with the second end of shared heat exchanger tube by outlet pipe;Flowline connects the air inlet of vavuum pump;Ball valve is provided with oil inlet pipe, flowline, water inlet pipe and outlet pipe.The production of resins cooling system that the utility model is provided, by rational structure setting, deep fat heating and thermal insulation state quickly can be switched to cold water cooling, and two sets of heat-exchange systems share a set of heat exchange pipeline, deep fat can be removed totally by the principle of reduction vaporization, not influence water circulation system.

Description

A kind of production of resins cooling system
Technical field
The utility model is related to athletic floor field, more particularly to a kind of production of resins cooling system.
Background technology
The floor on athletic ground usually requires elasticity that floor had-have certain shock-absorbing capacity, joint when preventing motion It is injured;The persistence that floor has had is needed, service life will be grown, and surface is wear-resisting;Good rigidity, floor elasticity can not be excessive Height, floor integrally stills need preferable rigidity, can support whole ground, will not occur too big deformation to meet various sports grounds The demand on ground;The feature of environmental protection, in recent years the report of malicious plastic cement race track also emerge in an endless stream, therefore used material safety and environmental protection be also must Want one of condition.
And in the prior art, the material of motion plastic floor is typically to have various raw materials to be reacted under certain condition after mixing The resin of generation, and the various material performances of production of resins process are different, and usually need quick changeable temperature processing suitable to obtain Reaction condition prepares the resin material for meeting and requiring, previous step needs to carry out insulation reaction at a temperature of 100 degree, But next step, which then needs to be down to room temperature, is reacted.And the reactor of conventional industries is typically profit to reaction system cooling Realized with heat exchanger, such one is that the power consumption of heat-exchange time length is high, and two be that cooling velocity is too slow, and this also results in many laboratories Can be with the good resin of processability, but the product prepared in pilot scale and industrialization debugging can not meet requirement.
Utility model content
For defect of the prior art, the utility model provides a kind of cooling rate fast production of resins cooling system.
The production of resins cooling system that the utility model is provided includes retort and cooling system, and the retort is chuck Formula retort;The cooling system includes sharing heat exchanger tube, and the shared heat exchanger tube is arranged in the heat exchanging interlayer of retort;Institute Stating cooling system also includes deep fat storage tank, cold oil storage tank, hot water storage tank and cold water storage tank;The cold oil storage tank and shared heat exchanger tube The first end of bottom is connected by oil inlet pipe, and the deep fat storage tank is connected with the second end at the top of shared heat exchanger tube by flowline It is logical;The cold water storage tank is connected with the first end of the heat exchanger tube by water inlet pipe, the hot water storage tank and the shared heat exchange Second end of pipe is connected by outlet pipe;The flowline connects the air inlet of vavuum pump;The oil inlet pipe, flowline, water inlet Ball valve is provided with pipe and outlet pipe.
It is deep fat when above needing soak to react, in heat exchanger tube, deep fat is through public heat exchanger tube and retort heat exchange Entered afterwards by flowline in deep fat storage tank, when needing rapid cooling, valve is opened, deep fat is returned cold by Action of Gravity Field In oil tank, but now there is the deep fat of residual in heat exchanger tube, by opening vavuum pump, using being evaporated under reduced pressure the oil in pipeline Evaporation is reclaimed, and now turns off the valve on oil inlet pipe and flowline, opens the valve on water inlet pipe and outlet pipe so that cold water Into in public heat exchanger tube heat exchange cooling is carried out with retort.
Further, it is less than the position of the first end height of heat exchanger tube described in above-mentioned production of resins cooling system on oil inlet pipe Put between cold oil storage tank it is in parallel enter oil inlet pipe, it is described enter oil inlet pipe on air inlet and ball valve are set.Because oil temperature is higher, pipeline and Valve is easily damaged, sets into oil inlet pipe for the ease of maintenance, in addition when vavuum pump is opened, what is set on oil inlet pipe is entered enters Gas port, which is allowed air to flow into, to be inhaled cleaner by the Residual oil in public heat exchanger tube, when vacuumizing, and extraneous cold air is simultaneously Into in public heat exchanger tube heat exchange cooling is carried out with retort.
Further, it is higher than the position of the second end height of heat exchanger tube described in above-mentioned production of resins cooling system on flowline Oil outlet branch pipe in parallel between the second end with heat exchanger tube is put, the vavuum pump is located in oil outlet branch pipe with flowline tie point;It is described Ball valve is provided with oil outlet branch pipe.This is regulation during beneficial to heating in order to produce loop in deep fat Heat preservation.
Further, oil recovery tank is provided between vavuum pump and flowline described in above-mentioned production of resins cooling system, The air-inlet of vacuum pump at the top of oil recovery tank with being connected, and the flowline is connected with oil recovery tank bottom.
In summary, the production of resins cooling system that the utility model is provided, can be quick by rational structure setting Deep fat heating and thermal insulation state is switched to cold water cooling, and two sets of heat-exchange systems share a set of heat exchange pipeline, are steamed by depressurizing The principle of hair can remove deep fat totally, not influence water circulation system.
Brief description of the drawings
, below will be right in order to illustrate more clearly of the utility model embodiment or technical scheme of the prior art The accompanying drawing used required in embodiment or description of the prior art is briefly described.In all of the figs, it is similar Element or part are general by similar reference mark.In accompanying drawing, each element or part might not be according to actual ratios Draw.
The principle schematic for the production of resins cooling system that Fig. 1 provides for the embodiment of the utility model one.
Embodiment
The embodiment of technical solutions of the utility model is described in detail below in conjunction with accompanying drawing.Following examples are only For clearly illustrating the technical solution of the utility model, therefore example is only used as, and this practicality can not be limited with this New protection domain.
It should be noted that unless otherwise indicated, technical term or scientific terminology used in this application should be this reality The ordinary meaning understood with new one of ordinary skill in the art.
In the description of the present application, it is to be understood that term " under ", " top ", " bottom ", " height ", the side of the instruction such as " low " Position or position relationship are, based on orientation shown in the drawings or position relationship, to be for only for ease of description the utility model and simplification is retouched State, rather than indicate or imply that the device or element of meaning there must be specific orientation, with specific azimuth configuration and operation, Therefore it is not intended that to limitation of the present utility model.
In addition, term " first ", " second " etc. are only used for describing purpose, and it is not intended that indicating or implying relatively important Property or the implicit quantity for indicating indicated technical characteristic.In description of the present utility model, " multiple " are meant that two More than, unless otherwise specifically defined.
In this application, unless otherwise clearly defined and limited, term " connection " should be interpreted broadly, for example, can be with It is to be fixedly connected or be detachably connected, or integrally;Can be mechanical connection or pipeline connection;Can be Be joined directly together, can also be indirectly connected to by intermediary, can be two element internals connection or two elements it is mutual Interactively.For the ordinary skill in the art, it can understand that above-mentioned term is new in this practicality as the case may be Concrete meaning in type.
The utility model is described as follows the preferred embodiment provided according to Fig. 1:
Production of resins cooling system includes retort 1 and cooling system, and the retort 1 is jacket type retort 1;It is described Cooling system includes sharing heat exchanger tube 2, and the shared heat exchanger tube 2 is arranged in the heat exchanging interlayer of retort 1;The cooling system Also include deep fat storage tank 16, cold oil storage tank 11, hot water storage tank 24 and cold water storage tank 21;The cold oil storage tank 11 and shared heat exchanger tube The first end of 2 bottoms is connected by oil inlet pipe 12, and the second end at the top of the deep fat storage tank 16 and shared heat exchanger tube 2 passes through fuel-displaced Pipe 15 is connected;The cold water storage tank 21 is connected with the first end of the heat exchanger tube by water inlet pipe 22, the hot water storage tank 24 with Second end of the shared heat exchanger tube 2 is connected by outlet pipe 23;The flowline 15 connects the air inlet of vavuum pump 3;It is described Ball valve is provided with oil inlet pipe 12, flowline 15, water inlet pipe 22 and outlet pipe 23.
It is high temperature oil medium in public heat exchanger tube, deep fat is through public heat exchanger tube when reaction system needs the soak to react Entered after being exchanged heat with retort 1 by flowline 15 in deep fat storage tank 16, when needing rapid cooling, valve is opened, deep fat Returned by Action of Gravity Field in cold oil storage tank 11, but now also have the deep fat of residual, by opening vavuum pump 3, profit in heat exchanger tube The oil evaporation in pipeline is reclaimed with being evaporated under reduced pressure, the valve on oil inlet pipe 12 and flowline 15 is now turned off, opens water inlet Valve on pipe 22 and outlet pipe 23 so that cold water enter public heat exchanger tube in retort 1 carry out heat exchange cooling.
On oil inlet pipe 12 less than heat exchanger tube first end height position it is in parallel between cold oil storage tank 11 enter oil inlet pipe 13, institute State and be provided with ball valve on oil inlet pipe 13;On flowline 15 higher than heat exchanger tube the second end height position and heat exchanger tube second Oil outlet branch pipe 14 in parallel between end, the vavuum pump 3 is located in oil outlet branch pipe 14 with the tie point of flowline 15;The oil outlet branch pipe 14 On be provided with ball valve.Oil recovery tank, the air inlet of vavuum pump 3 and oil recovery tank are provided between vavuum pump 3 and flowline 15 Top is connected, and the flowline 15 is connected with oil recovery tank bottom.
Above-mentioned public heat exchanger tube can be coil pipe, not straight tube as illustrated in the drawing, for ease of understanding, be alkalized into straight Pipe is shown in Fig. 1.
Finally it should be noted that:Various embodiments above is only limited to illustrate the technical solution of the utility model, rather than to it System;Although the utility model is described in detail with reference to foregoing embodiments, one of ordinary skill in the art should Understand:It can still modify to the technical scheme described in foregoing embodiments, or to which part or whole Technical characteristic carries out equivalent substitution;And these modifications or replacement, the essence of appropriate technical solution is departed from this practicality newly The scope of each embodiment technical scheme of type, it all should cover among claim of the present utility model and the scope of specification.

Claims (4)

1. a kind of production of resins cooling system, it is characterised in that including:
Retort and cooling system, the retort are jacket type retort;
The cooling system includes sharing heat exchanger tube, and the shared heat exchanger tube is arranged in the heat exchanging interlayer of retort;
The cooling system also includes deep fat storage tank, cold oil storage tank, hot water storage tank and cold water storage tank;
The cold oil storage tank is connected with the first end of shared heat exchanger tube bottom by oil inlet pipe, and the deep fat storage tank is with sharing heat exchange Second end in tube top portion is connected by flowline;
The cold water storage tank is connected with the first end of the heat exchanger tube by water inlet pipe, the hot water storage tank and the shared heat exchange Second end of pipe is connected by outlet pipe;
The flowline connects the air inlet of vavuum pump;
Ball valve is provided with the oil inlet pipe, flowline, water inlet pipe and outlet pipe.
2. production of resins cooling system according to claim 1, it is characterised in that
On the oil inlet pipe less than heat exchanger tube first end height position it is in parallel between cold oil storage tank enter oil inlet pipe, the oil-feed Air inlet and ball valve are set on branch pipe.
3. production of resins cooling system according to claim 1, it is characterised in that
The position of the second end height higher than heat exchanger tube and oil outlet branch pipe in parallel, institute between the second end of heat exchanger tube on the flowline Vavuum pump is stated with flowline tie point to be located in oil outlet branch pipe;Ball valve is provided with the oil outlet branch pipe.
4. production of resins cooling system according to claim 1, it is characterised in that
Oil recovery tank is provided between the vavuum pump and flowline, the air-inlet of vacuum pump is connected with oil recovery tank top, The flowline is connected with oil recovery tank bottom.
CN201720030513.6U 2017-01-11 2017-01-11 A kind of production of resins cooling system Expired - Fee Related CN206561617U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720030513.6U CN206561617U (en) 2017-01-11 2017-01-11 A kind of production of resins cooling system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720030513.6U CN206561617U (en) 2017-01-11 2017-01-11 A kind of production of resins cooling system

Publications (1)

Publication Number Publication Date
CN206561617U true CN206561617U (en) 2017-10-17

Family

ID=60028858

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720030513.6U Expired - Fee Related CN206561617U (en) 2017-01-11 2017-01-11 A kind of production of resins cooling system

Country Status (1)

Country Link
CN (1) CN206561617U (en)

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Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20171017

Termination date: 20220111

CF01 Termination of patent right due to non-payment of annual fee