CN204409549U - A kind of sticky material on-line continuous heater - Google Patents
A kind of sticky material on-line continuous heater Download PDFInfo
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- CN204409549U CN204409549U CN201520016703.3U CN201520016703U CN204409549U CN 204409549 U CN204409549 U CN 204409549U CN 201520016703 U CN201520016703 U CN 201520016703U CN 204409549 U CN204409549 U CN 204409549U
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- heat exchanger
- heater
- pipeline
- line continuous
- sticky material
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Abstract
The utility model provides a kind of sticky material on-line continuous heater, comprise controller, surge tank, First Heat Exchanger, the second heat exchanger, agitator tank, primary heater and secondary heater, described surge tank, First Heat Exchanger, agitator tank are communicated with by pipeline successively with the second heat exchanger, described First Heat Exchanger is connected with described primary heater, described second heat exchanger is connected with described secondary heater, and described controller is connected with described pipeline.Compared with prior art, the utility model can realize homogeneous heating, promotes heating effect, shorten the heat time, lowers energy consumption, enhances productivity.
Description
Technical field
The utility model relates to the sticky material heating technique in field of food, particularly thickness band granule materials on-line continuous heating and cooking technology, specifically a kind of sticky material on-line continuous heater.
Background technology
Heating uses the means of production the most general during modern industry is produced, and have different firing equipments and mode of heating, and optimum heating-up temperature needed for different heating targets and mode of heating all can have a great difference according to different heating targets.
The mode of heating of existing sticky material is generally fed intake together by various material, be placed on a boiling container, first mix, then carry out heating and cooking, this technology is method the most frequently used at present, its subject matter has: 1, the contact area of material and heating agent is little, heating process is uneven, heating effect is poor, cause heating energy consumption large, production efficiency is low; 2, boiling container is generally larger, and take up room comparatively large, equipment supporting during design of workshop is also more.
Utility model content
For above-mentioned defect of the prior art, the purpose of this utility model is to provide a kind of sticky material on-line continuous heater, can realize homogeneous heating, promotes heating effect, shorten the heat time, lower energy consumption, enhance productivity.
A kind of sticky material on-line continuous heater that the utility model provides, comprise controller, surge tank, First Heat Exchanger, the second heat exchanger, agitator tank, primary heater and secondary heater, described surge tank, First Heat Exchanger, agitator tank are communicated with by pipeline successively with the second heat exchanger, described First Heat Exchanger is connected with described primary heater, described second heat exchanger is connected with described secondary heater, and described controller is connected with described pipeline.
Preferably, comprise the 3rd heat exchanger, the 4th heat exchanger and heat-energy recovering apparatus, described 3rd heat exchanger, the 4th heat exchanger and heat-energy recovering apparatus are in turn connected to form loop by pipeline, described 3rd heat exchanger is connected with described First Heat Exchanger and described surge tank respectively by pipeline, and described 4th heat exchanger is connected with described second heat exchanger by pipeline.
Preferably, described sticky material on-line continuous heater also comprises maintaining manages, and described maintenance pipe one end connects described 4th heat exchanger, and the other end of described maintenance pipe is connected with described second heat exchanger by pipeline.
Preferably, described controller is automatic detection and control system, and described automatic detection and control system comprises temperature-detecting device, flow detector, pressure-detecting device and liquid level detection device.
Preferably, described primary heater and described secondary heater are hotline heater.
Preferably, described First Heat Exchanger and described hotline heater are connected to form loop, and described second heat exchanger is connected with described hotline heater and forms loop.
Preferably, the pipeline between described surge tank and described agitator tank is also provided with the compression pump for material transferring.
Preferably, the pipeline between described second heat exchanger and described agitator tank is also provided with the compression pump for material transferring.
Preferably, the pipeline between described heat-energy recovering apparatus and described 4th heat exchanger is also provided with the compression pump for transmitting temperature conduction medium.
Preferably, described sticky material on-line continuous heater is also provided with CIP purging system.
As can be seen from the above technical solutions, the utility model embodiment has the following advantages:
A kind of sticky material on-line continuous heater that the utility model provides, by arranging sticky material heat exchanger, heater forms hot systems, change foodstuffs industry band particle sticky material batch heating mode, by procedure heating design, realize the object of the on-line continuous heating of sticky material, this on-line continuous mode of heating can meet quantity-produced requirement in enormous quantities, improve production efficiency, ensure that the uniformity of product, reduce product quality fluctuation, by emphasis parameter detecting, achieve the automatically-monitored of product quality, greatly reduce the artificial frequency detected, simultaneously, it is abundant that the on-line continuous mode of heating that the utility model provides can realize homogeneous heating, improve the utilization rate of heat energy, reduce heat energy loss.
Accompanying drawing explanation
A kind of annexation schematic diagram of sticky material on-line continuous heater of Fig. 1 for providing in the utility model embodiment.
Detailed description of the invention
The following stated be preferred embodiment of the present utility model, what the utility model was protected is not limited to following preferred embodiment.It should be pointed out that the some distortion made and improvement, all belong to protection domain of the present utility model for a person skilled in the art on the basis that this utility model creates design.
A kind of sticky material on-line continuous heater that the utility model provides, see Fig. 1, comprise for automatically detecting and the controller of liquid level in control device in temperature of charge, pressure, flow and corresponding tank body, in this controller, multiple function element is set, as detector unit, flow detecting element, pressure detecting element and level sensing element etc., for the surge tank 1 of splendid attire material, for realizing heat exchanger material being carried out to exchange heat and transmission, according to technique needs, heat exchanger quantity can increase arbitrarily or reduce, in the present embodiment, two heat exchanger apparatus are set in the pipeline that material is heated, i.e. First Heat Exchanger 3 and the second heat exchanger 4, for the agitator tank 2 that the material of drawing from surge tank 1 and unclassified stores are carried out being uniformly mixed, for the heater heated material, it is public that a heater both can be set in the present embodiment, also can arrange multiple, in order to the convenience that heats and the effect ensureing heating, primary heater 5 and secondary heater 6 are set in the present embodiment, wherein, surge tank 1, First Heat Exchanger 3, agitator tank 2 is connected by pipeline 10 successively with the second heat exchanger 4, First Heat Exchanger 3 is connected with primary heater 5, second heat exchanger 4 is connected with secondary heater 6, generally undertaken being communicated with by heat exchanging pipe and carry out heat exchange, First Heat Exchanger 3 and primary heater 5 in the present embodiment, second heat exchanger 4 and secondary heater 6 are all communicated with by heat exchanging pipe and form heat exchange loop, namely First Heat Exchanger 3 and primary heater 5 are connected to form the first heat exchange loop 19, second heat exchanger 4 is connected to form the second heat exchange loop 20 with secondary heater 6, automatic detection and control system is chosen as controller in the utility model embodiment, controller is by being arranged in system pipeline by some building blocks of function elements wherein, as by detector unit wherein, flow detecting element, pressure detecting element and liquid level detection device element are on pipeline 10, the automatic control to whole heating system is realized while being connected with this on-line continuous heater.
In order to economize energy better with realize heat and make full use of, the sticky material on-line continuous heater provided in the utility model embodiment is provided with the 3rd heat exchanger 7, the 4th heat exchanger 8 and heat-energy recovering apparatus 9, form a heat energy recycle pipeline, namely the 3rd heat exchanger 7, the 4th heat exchanger 8 and heat-energy recovering apparatus 9 are in turn connected to form the loop of an energy recovery and re-using by heat energy recovery pipeline 18.And, 3rd heat exchanger 7 is connected with First Heat Exchanger 3 and surge tank 1 respectively by pipeline 10, namely the 3rd heat exchanger 7 is arranged on the pipeline between First Heat Exchanger 3 and surge tank 1, 4th heat exchanger 8 is connected with the second heat exchanger 4 by pipeline 10, realize the continuous transmission of material, and, in order to ensure local flavor and the sterilization effect of material, also be connected with between the second heat exchanger 4 and the 4th heat exchanger 8 and maintain pipe 16, and this maintenance pipe 16 is thin compared with the pipeline 10 in the utility model embodiment, this maintenance pipe 16 one end with and the pipeline 10 that is connected of the second heat exchanger 4 connect, maintain pipe 16 other end to be connected with the 4th heat exchanger 8, simultaneously, 4th heat exchanger 8 is by heat energy recovery pipeline 18, namely temperature conduction medium pipeline is connected with heat-energy recovering apparatus 9, by above-mentioned design, when material carries out cooling process through the 4th heat exchanger 8, lower the temperature qualified can discharge pipe 17 discharging of sticky material by being connected with the 4th heat exchanger of discharging, and the heat shed in temperature-fall period is collected into heat-energy recovering apparatus 9 by heat energy recovery pipeline 18, then transfer in the 3rd heat exchanger 7 by heat energy recovery pipeline 18, for heating the material flowed out from surge tank 1, realize the recycling of heat energy, simultaneously, temperature conduction medium in heat energy recovery pipeline 18 is after the heat absorption of the 3rd heat exchanger 7 exchanges, become refrigerant exchange media, the 4th heat exchanger 8 is transferred to again by heat energy recovery pipeline 18, through the 4th heat exchanger 8 to the material of discharging carrying out heat exchange, temperature is collected and is transferred to heat-energy recovering apparatus 9, thus form a thermal energy exchange and recycle pipeline.
In the utility model embodiment, in order to heat material better, realize heat conducting all even stable, choose hotline heater as primary heater 5 and secondary heater 6, hotline heater can be one, also can be two, two hotline heaters are chosen in the present embodiment, wherein First Heat Exchanger 3 is connected with the first hotline heater loop, second heat exchanger 4 and the second hotline heater are also that loop is connected, by heat transfer and the exchange of hotline heater, realize the thermally equivalent to flowing through material.
More smooth and easy and controlled in order to what make material and temperature conduction medium transmit in pipeline 10, pipeline 10 between surge tank 1 and agitator tank 2 is provided with for the product pump 11 to raw material pressurized transfer, pipeline 10 between the second heat exchanger 4 and agitator tank 2 is provided with the pump 21 for carrying out pressurized transfer to the material after stirring, heat energy recovery pipeline 18 between heat-energy recovering apparatus 9 and the 4th heat exchanger 8 is provided with the compression pump 22 for transmitting temperature conduction medium, generally arranging one at corresponding position can realize corresponding pressurization function, also can arrange multiple according to the viscosity of material.
For ensureing system food sanitation safe, CIP purging system is also provided with in the on-line heating device that the utility model embodiment provides, this purging system enters from the material inlet surge tank 1, the finished product materials last from system exports away, loop is formed with CIP, according to the production cycle, pipeline situation, material characteristic etc., concentration and the scavenging period of CIP cleaning fluid are set, realize cleaning automatically, because the flow designed between this equipment pipe mates mutually, so whole system is as same pipeline, so pipeline loop in heater can be cleaned without dead angle, thus realize health and the safety of food.
For being described the annexation of each assembly of heater that the utility model embodiment provides more intuitively, be described from concrete production procedure angle below:
In process of production, first some setting parameters are carried out for the material being about to produce, comprise temperature, pressure, liquid level etc. in flow and related device is preset, then raw material is entered surge tank 1 by material inlet, the recovery heat transmitted by heat energy recovery pipeline 18 in the 3rd heat exchanger 7 is utilized to carry out preheating, when the shortage of heat in the 3rd heat exchanger 7 with by heating material to setting temperature time, this is not enough temperature section utilizes in primary heater 5 heat energy, this material is heated by the first heat exchange loop 19 by the conduction oil heat in the first conduction oil in the present embodiment.When the first detector unit 12 by being arranged near First Heat Exchanger on pipeline 10, first pressure detecting element 13, first flow detecting element 14 detects the material after this heating, after terms and conditions all reaches the condition of setting, after the first level sensing element 15 in surge tank detects that the liquid level of surge tank arrives certain position, by being arranged on product pump 11 pump in surge tank 1 lower pipeline 10 to agitator tank 2, simultaneously according to Production requirement, itself and material is added by the material inlet on agitator tank 2, material after adding is uniformly mixed.When the liquid level detected in agitator tank 2 when the second level sensing element 27 on agitator tank 2 after mixing arrives certain liquid level, by being arranged on pump 21 pump between agitator tank 2 and the second heat exchanger 4 on pipeline 10 in the second heat exchanger 4, utilize secondary heater 6, the high temperature (150 ~ 250 degrees Celsius) of the conduction oil namely heated in the second hotline heater is by the second heat exchange loop 20, instantaneous mixed material in second heat exchanger 6 is heated to design temperature, when the second detector unit 24 by being arranged on the second heat exchanger 6 annex pipeline 10, second pressure detecting element 25, second flow detecting element 26 carries out detecting to the material after this heating and after terms and conditions reaches the condition of setting, by the maintenance pipe 16 be connected with the second heat exchanger 6, material is imported the 4th heat exchanger 8, utilize the temperature conduction medium in heat energy recovery pipeline 18, namely refrigerant is cooled by the 4th heat exchanger 8 pairs of materials, reach finished product materials temperature requirement and get final product discharging, simultaneously, the energy that refrigerant is obtained by heat exchange in the 4th heat exchanger 8 is first collected in heat reclaim unit 9, when the 3rd level sensing element 23 on heat-energy recovering apparatus 9 detects that the liquid level in heat-energy recovering apparatus 9 arrives certain liquid level, be used for reclaiming heat transfer to the 3rd heat exchanger 7 material that preheating newly adds by the compression pump 22 on heat energy recovery pipeline 18, realize the object of energy regenerating, reduce energy consumption.
The on-line continuous heater that the utility model provides is suitable for the laser heating production etc. that particle tartar sauce was produced, was with to the laser heating of tartar sauce.
Above, by arranging sticky material heat exchanger, heater forms hot systems, change foodstuffs industry band particle sticky material batch heating mode, by procedure heating design, realize the object of the on-line continuous heating of sticky material, this on-line continuous mode of heating can meet quantity-produced requirement in enormous quantities, improve production efficiency, ensure that the uniformity of product, reduce product quality fluctuation, by emphasis parameter detecting, achieve the automatically-monitored of product quality, greatly reduce the artificial frequency detected, simultaneously, it is abundant that the on-line continuous mode of heating that the utility model provides can realize homogeneous heating, improve the utilization rate of heat energy, reduce heat energy loss.On-line continuous heater realizes constant flux control automatically, and sterilising temp is adjustable, and Fast-Balance, realize speed adjustable, temperature can control, and meets the production requirement of multiple product to greatest extent; Meanwhile, CIP purging system can arrange concentration and the scavenging period of CIP cleaning fluid according to production cycle, pipeline situation, material characteristic etc., ensures system food sanitation safe.The mode of the jacketed pan used in a large number with existing industry is compared, and on-line continuous mode of heating improves the integrated automation level of production, reduces energy consumption, and energy consumption reduces by 10 ~ 30%.Production efficiency at least improves 50%, and some material even can improve 50%, and in same production capacity situation, minimizing more than 50% is taken up an area in workshop.
The above, above embodiment only in order to the technical solution of the utility model to be described, is not intended to limit; Although be described in detail the utility model with reference to previous embodiment, those of ordinary skill in the art is to be understood that: it still can be modified to the technical scheme described in foregoing embodiments, or carries out equivalent replacement to wherein portion of techniques feature; And these amendments or replacement, do not make the essence of appropriate technical solution depart from the spirit and scope of each embodiment technical scheme of the utility model.
Claims (10)
1. a sticky material on-line continuous heater, it is characterized in that, comprise controller, surge tank, First Heat Exchanger, the second heat exchanger, agitator tank, primary heater and secondary heater, described surge tank, First Heat Exchanger, agitator tank are communicated with by pipeline successively with the second heat exchanger, described First Heat Exchanger is connected with described primary heater, described second heat exchanger is connected with described secondary heater, and described controller is connected with described pipeline.
2. a kind of sticky material on-line continuous heater as claimed in claim 1, it is characterized in that, comprise the 3rd heat exchanger, the 4th heat exchanger and heat-energy recovering apparatus, described 3rd heat exchanger, the 4th heat exchanger and heat-energy recovering apparatus are in turn connected to form loop by pipeline, described 3rd heat exchanger is connected with described First Heat Exchanger and described surge tank respectively by pipeline, and described 4th heat exchanger is connected with described second heat exchanger by pipeline.
3. a kind of sticky material on-line continuous heater as claimed in claim 2, it is characterized in that, described sticky material on-line continuous heater also comprises maintaining manages, described maintenance pipe one end connects described 4th heat exchanger, and the other end of described maintenance pipe is connected with described second heat exchanger by pipeline.
4. a kind of sticky material on-line continuous heater as claimed in claim 1, it is characterized in that, described controller is automatic detection and control system, and described automatic detection and control system comprises temperature-detecting device, flow detector, pressure-detecting device and liquid level detection device.
5. a kind of sticky material on-line continuous heater as claimed in claim 1, it is characterized in that, described primary heater and described secondary heater are hotline heater.
6. a kind of sticky material on-line continuous heater as claimed in claim 5, it is characterized in that, described First Heat Exchanger and described hotline heater are connected to form loop, and described second heat exchanger is connected with described hotline heater and forms loop.
7. a kind of sticky material on-line continuous heater as claimed in claim 1, is characterized in that, the pipeline between described surge tank and described agitator tank is also provided with the compression pump for material transferring.
8. a kind of sticky material on-line continuous heater as claimed in claim 1, is characterized in that, the pipeline between described second heat exchanger and described agitator tank is also provided with the compression pump for material transferring.
9. a kind of sticky material on-line continuous heater as claimed in claim 2, is characterized in that, the pipeline between described heat-energy recovering apparatus and described 4th heat exchanger is also provided with the compression pump for transmitting temperature conduction medium.
10. a kind of sticky material on-line continuous heater as claimed in claim 1, is characterized in that, described sticky material on-line continuous heater is provided with CIP purging system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520016703.3U CN204409549U (en) | 2015-01-09 | 2015-01-09 | A kind of sticky material on-line continuous heater |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520016703.3U CN204409549U (en) | 2015-01-09 | 2015-01-09 | A kind of sticky material on-line continuous heater |
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| CN204409549U true CN204409549U (en) | 2015-06-24 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104489881A (en) * | 2015-01-09 | 2015-04-08 | 佛山市海天调味食品股份有限公司 | Online viscous material continuous heating device |
| CN109277007A (en) * | 2018-09-20 | 2019-01-29 | 佛山市海天（江苏）调味食品有限公司 | A kind of dissolution process of viscous material |
-
2015
- 2015-01-09 CN CN201520016703.3U patent/CN204409549U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104489881A (en) * | 2015-01-09 | 2015-04-08 | 佛山市海天调味食品股份有限公司 | Online viscous material continuous heating device |
| CN109277007A (en) * | 2018-09-20 | 2019-01-29 | 佛山市海天（江苏）调味食品有限公司 | A kind of dissolution process of viscous material |
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