CN104489881B - A kind of sticky material on-line continuous heater - Google Patents

A kind of sticky material on-line continuous heater Download PDF

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Publication number
CN104489881B
CN104489881B CN201510012629.2A CN201510012629A CN104489881B CN 104489881 B CN104489881 B CN 104489881B CN 201510012629 A CN201510012629 A CN 201510012629A CN 104489881 B CN104489881 B CN 104489881B
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heat exchanger
heater
pipeline
heat
line continuous
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CN201510012629.2A
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CN104489881A (en
Inventor
关俊杰
陈建义
徐艳娟
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Foshan Haitian Flavoring and Food Co Ltd
Foshan Haitian Gaoming Flavoring and Food Co Ltd
Foshan Haitian Jiangsu Flavoring and Food Co Ltd
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Foshan Haitian Flavoring and Food Co Ltd
Foshan Haitian Gaoming Flavoring and Food Co Ltd
Foshan Haitian Jiangsu Flavoring and Food Co Ltd
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Application filed by Foshan Haitian Flavoring and Food Co Ltd, Foshan Haitian Gaoming Flavoring and Food Co Ltd, Foshan Haitian Jiangsu Flavoring and Food Co Ltd filed Critical Foshan Haitian Flavoring and Food Co Ltd
Priority to CN201510012629.2A priority Critical patent/CN104489881B/en
Publication of CN104489881A publication Critical patent/CN104489881A/en
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  • Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
  • Instantaneous Water Boilers, Portable Hot-Water Supply Apparatuses, And Control Of Portable Hot-Water Supply Apparatuses (AREA)

Abstract

The invention provides a kind of sticky material on-line continuous heater, including 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 and the second heat exchanger pass sequentially through pipeline and connect, 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 present invention is capable of uniformly heating, promotes heats, shortens heat time heating time, lowers energy consumption, improves production efficiency etc..

Description

A kind of sticky material on-line continuous heater
Technical field
The present invention relates to the sticky material heating technique in field of food, particularly to thickness band granule materials On-line continuous heating and cooking technology, specifically a kind of sticky material on-line continuous heater.
Background technology
Heating is the means of production most commonly used during modern industry produces, according to different heating targets Have different firing equipments and a mode of heating, and the optimum heating-up temperature needed for different heating targets and Mode of heating all can be very different.
The mode of heating of existing sticky material is usually and is fed intake together by various materials, is placed on one Boiling container, first mixes, then carries out heating and cooking, and this technology is current most common method, and it is main Wanting problem to have: 1, material is little with the contact area of heating agent, heating process is uneven, heats is poor, make Become to add that thermal energy consumption is big, production efficiency is low;2, boiling container is larger, takes up room relatively big, car Between design time supporting equipment the most more.
Summary of the invention
For above-mentioned defect of the prior art, it is an object of the invention to provide a kind of sticky material online Continuous heating, it is possible to realize uniformly heating, lifting heats, shorten heat time heating time, lower energy Consumption, improves production efficiency etc..
The present invention provide a kind of sticky material on-line continuous heater, including 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 and the second heat exchanger pass sequentially through pipeline and connect, described First Heat Exchanger Being connected with described primary heater, described second heat exchanger is connected with described secondary heater, described control Device is connected with described pipeline.
Preferably, including the 3rd heat exchanger, the 4th heat exchanger and heat-energy recovering apparatus, described 3rd heat exchange Device, the 4th heat exchanger and heat-energy recovering apparatus are in turn connected to form loop, described 3rd heat exchange by pipeline Device is connected with described First Heat Exchanger and described surge tank respectively by pipeline, and described 4th heat exchanger passes through Pipeline is connected with described second heat exchanger.
Preferably, described sticky material on-line continuous heater also includes maintaining pipe, described maintenance pipe one End connects described 4th heat exchanger, and the other end of described maintenance pipe is by pipeline with described second heat exchanger even Connect.
Preferably, described controller is automatic detection and control system, and described automatic detection and control system includes 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 be connected with described hotline heater formation loop, 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 additionally provided with for material transferring Compression pump.
Preferably, the pipeline between described second heat exchanger and described agitator tank is additionally provided with for material The compression pump of transmission.
Preferably, the pipeline between described heat-energy recovering apparatus and described 4th heat exchanger is additionally provided with use Compression pump in transmission temperature conduction medium.
Preferably, described sticky material on-line continuous heater is additionally provided with CIP purging system.
As can be seen from the above technical solutions, the embodiment of the present invention has the advantage that
A kind of sticky material on-line continuous heater that the present invention provides, by arranging sticky material heat exchange Device, heater forms hot systems, changes foodstuffs industry band granule sticky material batch heating mode, By procedure heating design, it is achieved the purpose of the on-line continuous heating of sticky material, this on-line continuous adds Hot mode disclosure satisfy that high-volume quantity-produced requirement, improves production efficiency, ensure that the system of product One property, reduces product quality fluctuation, by emphasis parameter detecting, it is achieved that the automatization of product quality Monitoring, greatly reduces the frequency of artificial detection, meanwhile, the on-line continuous mode of heating that the present invention provides It is capable of homogeneous heating abundant, improves the utilization rate of heat energy, reduce heat energy loss.
Accompanying drawing explanation
One company of the Fig. 1 a kind of sticky material on-line continuous heater for providing in the embodiment of the present invention Connect relation schematic diagram.
Detailed description of the invention
The following stated is the preferred embodiment of the present invention, what the present invention was protected be not limited to following preferably Embodiment.It should be pointed out that, the basis conceived for a person skilled in the art in these innovation and creation On, the some deformation made and improvement, broadly fall into protection scope of the present invention.
A kind of sticky material on-line continuous heater that the present invention provides, sees Fig. 1, including for automatically Detect and control the controller of liquid level in temperature of charge in device, pressure, flow and corresponding tank body, This controller arranges multiple function element, such as detector unit, flow detecting element, pressure detecting Element and Level Detection element etc.;For containing the surge tank 1 of material, for realization, material being carried out heat Exchange and the heat exchanger transmitted, according to technique needs, heat exchanger quantity can arbitrarily be increased or decreased, this Embodiment arranges in the pipeline heating material two heat exchanger apparatus, i.e. First Heat Exchanger 3 With the second heat exchanger 4;For stirring of being stirred the material drawn from surge tank 1 with unclassified stores mixing Mix tank 2, for the heater that material is heated, the present embodiment both can arrange heater public affairs With, it is also possible to arrange multiple, for the convenience heated and the effect ensureing heating, the present embodiment is arranged Primary heater 5 and secondary heater 6, wherein, surge tank 1, First Heat Exchanger 3, agitator tank 2 and Second heat exchanger 4 passes sequentially through pipeline 10 and is attached, First Heat Exchanger 3 is connected with primary heater 5, Second heat exchanger 4 is connected with secondary heater 6, connects generally by heat exchanging pipe and carries out Heat exchange, First Heat Exchanger 3 and primary heater the 5, second heat exchanger 4 and the second heating in the present embodiment Device 6 all forms heat exchange loop, i.e. First Heat Exchanger 3 and primary heater 5 by heat exchanging pipe connection Connecting and form the first heat exchange loop 19, the second heat exchanger 4 is connected formation the second heat with secondary heater 6 Exchange loop 20, chooses automatic detection and control system and leads to as controller, controller in the embodiment of the present invention Cross some of which building blocks of function element is arranged in system pipeline, as by detector unit therein, Flow detecting element, pressure detecting element and liquid level detection device element are on pipeline 10, online with this Continuous heating realizes automatically controlling whole heating system while connecting.
In order to preferably save the energy and realize heat and make full use of, the thickness provided in the embodiment of the present invention Material on-line continuous heater is provided with the 3rd heat exchanger the 7, the 4th heat exchanger 8 and heat-energy recovering apparatus 9, Form a heat energy recycle pipeline, the i.e. the 3rd heat exchanger the 7, the 4th heat exchanger 8 and energy recovery dress Put 9 and be in turn connected to form an energy recovery and the loop of re-using by heat energy recovery pipeline 18.And And, the 3rd heat exchanger 7 is connected with First Heat Exchanger 3 and surge tank 1 respectively by pipeline 10, and the i.e. the 3rd Heat exchanger 7 is arranged on the pipeline between First Heat Exchanger 3 and surge tank 1, and the 4th heat exchanger 8 passes through Pipeline 10 is connected with the second heat exchanger 4, it is achieved continuously transmitting of material, and, in order to ensure material Local flavor and sterilization effect, be also associated with maintaining pipe 16 between the second heat exchanger 4 and the 4th heat exchanger 8, And pipeline in this maintenance pipe 16 relatively embodiment of the present invention 10 is thin, this maintenance pipe 16 one end with and second change The pipeline 10 that hot device 4 connects is attached, and maintains pipe 16 other end and the 4th heat exchanger 8 to connect;With Time, the 4th heat exchanger 8 is filled with energy recovery by heat energy recovery pipeline 18, i.e. temperature conduction medium pipeline Put 9 connections, by above-mentioned design, when material carries out cooling process through the 4th heat exchanger 8, cooling Qualified can with the sticky material of discharging by discharge pipe 17 discharging being connected with the 4th heat exchanger, and fall The heat shed during temperature is collected to heat-energy recovering apparatus 9 by heat energy recovery pipeline 18, then passes through Heat energy recovery pipeline 18 transmits to the 3rd heat exchanger 7, for entering the material flowed out from surge tank 1 Row heating, it is achieved the recycling of heat energy, meanwhile, the temperature conduction medium warp in heat energy recovery pipeline 18 After the heat absorption exchange of the 3rd heat exchanger 7, become coolant exchange media, further through heat energy recovery pipeline 18 transmission are to the 4th heat exchanger 8, through the 4th heat exchanger 8 to carrying out heat exchange with the material of discharging, Temperature collection is transferred to heat-energy recovering apparatus 9, thus forms a thermal energy exchange and recycle pipeline.
In the embodiment of the present invention, in order to preferably material be heated, it is achieved conduction of heat the most even surely Fixed, choose hotline heater as primary heater 5 and secondary heater 6, hotline heater is permissible It is one, it is also possible to be two, the present embodiment is chosen two hotline heaters, wherein the first heat exchange Device 3 is connected with the first hotline heater loop, and the second heat exchanger 4 with the second hotline heater is also Loop connects, by conduction of heat and the exchange of hotline heater, it is achieved to the thermally equivalent flowing through material.
So that material and temperature conduction medium transmit in pipeline 10 more smoothly and controlled, slow Rush be provided with on the pipeline 10 between tank 1 and agitator tank 2 for the product pump 11 of raw material pressurized transfer, It is provided with on pipeline 10 between the second heat exchanger 4 and agitator tank 2 for the material after agitated is entered The pump 21 of row pressurized transfer, the heat energy recovery pipeline between heat-energy recovering apparatus 9 and the 4th heat exchanger 8 It is provided with the compression pump 22 for transmitting temperature conduction medium on 18, typically arranges one at corresponding position Corresponding pressurization function can be realized, it is also possible to arrange multiple according to the viscosity of material.
For ensureing system food sanitation safe, also set in the on-line heating device that the embodiment of the present invention provides Being equipped with CIP purging system, this purging system material inlet from surge tank 1 enters, last from system Finished product materials export away, form loop with CIP, special according to production cycle, pipeline situation, material Property etc., concentration and the scavenging period of CIP cleanout fluid are set, it is achieved automatically clean, due to this equipment pipe Between road, the flow of design is mutually matched, so whole system such as same pipeline, it is possible to without dead angle Ground cleans the pipeline loop in heater, thus realizes health and the safety of food.
For the most intuitively the annexation of each assembly of heater that the embodiment of the present invention provides being carried out Illustrate, be described from concrete production procedure angle below:
In process of production, carry out some parameter settings first against the material that will produce, including temperature, Liquid level etc. in pressure, flow and related device is preset, and is then entered by material inlet by raw material Enter surge tank 1, carried out by the recovery heat of heat energy recovery pipeline 18 transmission in utilizing the 3rd heat exchanger 7 Preheating, when the shortage of heat in the 3rd heat exchanger 7 to be heated to the temperature set by material, this deficiency It is by leading in the first conduction oil that temperature section utilizes in the heat energy in primary heater 5, the present embodiment This material is heated by deep fat heat by the first heat exchange loop 19.When by being arranged on the first heat exchange First detector unit the 12, first pressure detecting element 13 on pipeline 10, first flow near device Material after this heating is detected by detecting element 14, after terms and conditions all reaches the condition set, when After the first Level Detection element 15 in surge tank detects that the liquid level of surge tank arrives certain position, By product pump 11 pump that is arranged in surge tank 1 lower pipeline 10 to agitator tank 2, simultaneously according to production Demand, adds itself and material by the material inlet on agitator tank 2, and the material after adding is stirred Mixing.Liquid level in the second Level Detection element 27 on agitator tank 2 detects agitator tank 2 after mixing When arriving certain liquid level, by the pump 21 being arranged between agitator tank 2 and the second heat exchanger 4 on pipeline 10 Pump in the second heat exchanger 4, utilizes the heat conduction of heating in secondary heater 6, the i.e. second hotline heater The high temperature (150~250 degrees Celsius) of oil is by the second heat exchange loop 20, instantaneous by the second heat exchanger 6 In mixed material be heated to design temperature, when by being arranged on the second heat exchanger 6 adnexa pipeline 10 This is added by second detector unit the 24, second pressure detecting element 25, second flow detecting element 26 After material after heat carries out detecting and terms and conditions reaches the condition set, by with the second heat exchanger 6 even The maintenance pipe 16 connect, imports the 4th heat exchanger 8 by material, utilizes the temperature in heat energy recovery pipeline 18 to pass Lead medium, i.e. coolant by the 4th heat exchanger 8, material to be cooled down, reach finished product materials temperature requirement Getting final product discharging, meanwhile, the energy that coolant is obtained by heat exchange in the 4th heat exchanger 8 is first collected to heat In retracting device 9, when the 3rd Level Detection element 23 on heat-energy recovering apparatus 9 detects energy recovery Liquid level in device 9 arrives certain liquid level, will be reclaimed by the compression pump 22 on heat energy recovery pipeline 18 Heat energy transmission is used for preheating the material being newly added to the 3rd heat exchanger 7, it is achieved the purpose of energy regenerating, fall Low energy consumption.
The on-line continuous heater that the present invention provides is suitable for the laser heating production of tartar sauce, band granule The laser heating production etc. of tartar sauce.
Above, by arranging sticky material heat exchanger, heater forms hot systems, changes foodstuffs row Industrial belt granule sticky material batch heating mode, by procedure heating design, it is achieved sticky material The purpose of line laser heating, this on-line continuous mode of heating disclosure satisfy that high-volume quantity-produced requirement, Improve production efficiency, ensure that the uniformity of product, reduce product quality fluctuation, joined by emphasis Number detection, it is achieved that product quality automatically-monitored, greatly reduces the frequency of artificial detection, meanwhile, It is abundant that the on-line continuous mode of heating that the present invention provides is capable of homogeneous heating, improve heat energy utilization rate, Reduce heat energy loss.On-line continuous heater is automatically obtained constant flux control, sterilising temp scalable, And Fast-Balance, it is achieved speed scalable, temperature can control, and meets multiple product to greatest extent Production requirement;Meanwhile, CIP purging system can set according to production cycle, pipeline situation, material characteristic etc. Put concentration and the scavenging period of CIP cleanout fluid, it is ensured that system food sanitation safe.Big compared with industry The mode of the jacketed pan that amount uses is compared, and on-line continuous mode of heating improves the integrated automation water of production Flat, reduce energy consumption, energy consumption reduces by 10~30%.Production efficiency at least improves 50%, and some material even may be used To improve 50%, and in the case of same production capacity, minimizing more than 50% is taken up an area in workshop.
The above, above example only in order to technical scheme to be described, is not intended to limit; Although being described in detail the present invention with reference to previous embodiment, those of ordinary skill in the art should Work as understanding: the technical scheme described in foregoing embodiments still can be modified by it, or to it Middle part technical characteristic carries out equivalent;And these amendments or replacement, do not make appropriate technical solution Essence depart from various embodiments of the present invention technical scheme spirit and scope.

Claims (9)

1. a sticky material on-line continuous heater, it is characterised in that include 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 and the second heat exchanger pass sequentially through pipeline and connect, described First Heat Exchanger Being connected with described primary heater, described second heat exchanger is connected with described secondary heater, described control Device is connected with described pipeline;
It is provided with material inlet on described agitator tank;
Described controller is automatic detection and control system, and described automatic detection and control system includes temperature detection Device, flow detector, pressure-detecting device and liquid level detection device.
2. a kind of sticky material on-line continuous heater as claimed in claim 1, it is characterised in that Including the 3rd heat exchanger, the 4th heat exchanger and heat-energy recovering apparatus, described 3rd heat exchanger, the 4th heat exchange Device and heat-energy recovering apparatus are in turn connected to form loop by pipeline, and described 3rd heat exchanger is divided by pipeline Not being connected with described First Heat Exchanger and described surge tank, described 4th heat exchanger is by pipeline and described the Two heat exchangers connect.
3. a kind of sticky material on-line continuous heater as claimed in claim 2, it is characterised in that Described sticky material on-line continuous heater also includes maintaining pipe, and described maintenance pipe one end connects described the Four heat exchangers, 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 characterised in that Described primary heater and described secondary heater are hotline heater.
5. a kind of sticky material on-line continuous heater as claimed in claim 4, it is characterised in that Described First Heat Exchanger is connected formation loop with described hotline heater, and described second heat exchanger is with described Hotline heater connects and forms loop.
6. a kind of sticky material on-line continuous heater as claimed in claim 1, it is characterised in that The compression pump for material transferring it is additionally provided with on pipeline between described surge tank and described agitator tank.
7. a kind of sticky material on-line continuous heater as claimed in claim 1, it is characterised in that It is additionally provided with the pressure for material transferring on pipeline between described second heat exchanger and described agitator tank Pump.
8. a kind of sticky material on-line continuous heater as claimed in claim 2, it is characterised in that It is additionally provided with on pipeline between described heat-energy recovering apparatus and described 4th heat exchanger for transmitting temperature biography Lead the compression pump of medium.
9. a kind of sticky material on-line continuous heater as claimed in claim 1, it is characterised in that Described sticky material on-line continuous heater is provided with CIP purging system.
CN201510012629.2A 2015-01-09 2015-01-09 A kind of sticky material on-line continuous heater Active CN104489881B (en)

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CN106890578A (en) * 2015-12-17 2017-06-27 珠海格力智能装备有限公司 Urea for vehicle solution process units

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US4637936A (en) * 1984-08-10 1987-01-20 Marlen Research Corporation Aspetic food processing apparatus and method
WO2006137418A1 (en) * 2005-06-21 2006-12-28 Tomoda Selling & Sailing Co., Ltd. Superheated steam generating device, and methods of manufacturing and heating food using superheated steam
EP2316308B1 (en) * 2009-11-03 2012-08-29 Spaghettissimo International AG Device and method for discontinuous cooking preparation of portioned food items
CN102652543B (en) * 2012-05-22 2013-06-12 江南大学 Floating type liquid food material heating device
CN204409549U (en) * 2015-01-09 2015-06-24 佛山市海天调味食品股份有限公司 A kind of sticky material on-line continuous heater

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