CN204499329U - A kind of multifunction energy-saving high-temperature sterilization system - Google Patents
A kind of multifunction energy-saving high-temperature sterilization system Download PDFInfo
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- CN204499329U CN204499329U CN201520173464.2U CN201520173464U CN204499329U CN 204499329 U CN204499329 U CN 204499329U CN 201520173464 U CN201520173464 U CN 201520173464U CN 204499329 U CN204499329 U CN 204499329U
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- temperature sterilization
- temperature
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Abstract
The utility model discloses a kind of multifunction energy-saving high-temperature sterilization system, sterilizing tank body adopts thermal sterilization mode, high-temperature sterilization mechanism and heat exchange mechanism is provided with in sterilizing tank body, material enters in high-temperature sterilization mechanism from pan feeding pipeline and exports heat exchange mechanism to by after the instantaneous heat sterilization of the high-temperature steam entered from steam inlet, pre-heating system is connected with external also setting of sterilization tank, low temperature pan feeding is successively through pre-heating system, heat exchange mechanism, be delivered to high-temperature sterilization mechanism again, after high-temperature sterilization, material then passes through heat exchange mechanism successively, pre-heating system, after low temperature pan feeding and high-temperature sterilization material carry out step by step heat exchange make high-temperature sterilization after material lower the temperature, and preheating is carried out to low temperature pan feeding.The heat energy of the material after multifunction energy-saving high-temperature sterilization system recoveries described in the utility model utilizes sterilizing carries out preheating to the pan feeding of low temperature, significantly reduce the consumption of steam, water, improve the utilization ratio of the energy, reduce equipment power dissipation, energy-conserving and environment-protective, reduce production cost.
Description
Technical field
The utility model relates to sterilizing mechanical field, particularly relates to a kind of multifunction energy-saving high-temperature sterilization system.
Background technology
The liquid beverages such as the drinks in food production industry, milk and beverage all need to carry out high temperature sterilization, kill wherein all microorganisms so that storage, keeping, improve the shelf-life, prevent from going bad.The conventional sterilization mode of liquid towards drink adopts high-temperature steam to carry out, and while improving sterilising temp, shorten the sterilization treatment time, the melanoidin amount avoiding such as sugar and amino acid in drink to generate increases.Complete in whole sterilization process is instantaneous at high operating temperatures, the corrupt and rotten microorganism of material and gemma can be caused thoroughly to kill, meanwhile, save the original local flavor of food and nutritional labeling greatly.Generally before high temperature sterilization, preheating can be carried out to drink simultaneously, effectively can shorten the time of high-temperature sterilization after the pre-heat treatment, avoid active ingredient to be destroyed due to long-time high temperature; Also need drink cooling down as early as possible after high-temperature sterilization process, avoid the drink long active ingredient that makes nature cool time to be destroyed, usually can adopt the mode of tank or spray.The steam that the process need of whole sterilization treatment is a large amount of and water, energy resource consumption is large, and production cost is high.
Utility model content
The technical assignment of technical problem to be solved in the utility model and proposition improves prior art, a kind of multifunction energy-saving high-temperature sterilization system is provided, solve the steam of the sterilizer in current technology, water consumption is large, energy consumption is high, the problem that production cost is high.
For solving above technical problem, the technical solution of the utility model is:
A kind of multifunction energy-saving high-temperature sterilization system, comprise sterilizing tank body, it is characterized in that, described sterilizing tank body adopts thermal sterilization mode, high-temperature sterilization mechanism and heat exchange mechanism is provided with in sterilizing tank body, high-temperature sterilization mechanism is provided with steam inlet, condensation-water drain and pan feeding pipeline, material enters in high-temperature sterilization mechanism from pan feeding pipeline and exports heat exchange mechanism to by after the instantaneous heat sterilization of the high-temperature steam entered from steam inlet, pre-heating system is connected with external also setting of sterilization tank, low temperature pan feeding is successively through pre-heating system, heat exchange mechanism, be delivered to high-temperature sterilization mechanism again, after high-temperature sterilization, material then passes through heat exchange mechanism successively, pre-heating system, after low temperature pan feeding and high-temperature sterilization material carry out step by step heat exchange make high-temperature sterilization after material lower the temperature, and preheating is carried out to low temperature pan feeding.Multifunction energy-saving high-temperature sterilization system described in the utility model is high temperature sterilization medium with steam, and temperature is high, and sterilizing time is extremely short, bactericidal effect is remarkable, and the chemical change caused is few, and steam is easy to Cemented filling, homogeneous heating, easy temperature control system, the latent heat of condensation is large.And the utility model has higher temperature material after utilizing high-temperature sterilization carries out preheating to unpasteurized low temperature pan feeding, effectively utilize the waste heat of the material after high-temperature sterilization, without the need to adopting other energy (steam, water, electric energy etc.) again, preheating is carried out to low temperature pan feeding, improve the utilization ratio of the energy, reduce the energy consumption needed for sterilization treatment.Low temperature pan feeding, after the pre-heat treatment, effectively can shorten the time of high-temperature sterilization treatment, avoids active ingredient to be destroyed due to long-time high temperature; After sterilizing, high-temperature material utilizes low temperature pan feeding to cool, and without the need to re-using low-temperature receiver (water or frozen water etc.), has saved water consumption greatly, reduces production cost.
Further, described heat exchange mechanism comprises the one-level heat exchanger and two-stage heat exchanger that connect successively, after high-temperature sterilization, material is contrary with the throughput direction of low temperature pan feeding between one-level heat exchanger, two-stage heat exchanger, high-temperature material reverse flow between heat exchanger after low temperature pan feeding and sterilizing, step by step carry out heat exchange, after utilizing sterilizing to greatest extent to the greatest extent, the waste heat of high-temperature material carries out preheating to low temperature pan feeding, after making sterilizing, the temperature of material reduces as far as possible, and the temperature of low temperature pan feeding improves as far as possible, shorten the high-temperature sterilization processing time.
Further, described high-temperature sterilization mechanism, one-level heat exchanger and two-stage heat exchanger adopt bushing type heat exchange structure, heat exchanging pipe is tortuous in sterilizing tank body, tube-in-tube heat exchanger is a kind of pure adverse current type heat exchanger, can also choose suitable sectional dimension, to improve fluid velocity simultaneously, increase the heat transfer coefficient of two side liquids, therefore its heat-transfer effect is good, and economize energy is easy to clean.
Further, described pre-heating system adopts plate type heat exchanger, the runner of plate type heat exchanger is little, plate is waveform, changes of section is complicated, the flow direction of fluid and flow velocity are constantly changed, add the disturbance of fluid, thus turbulent flow can be issued at very little flow velocity, there is higher heat transfer coefficient, in plate type heat exchanger, two kinds of media are almost full counter-current flow, and high heat-transfer effect, the minimum temperature difference of plate type heat exchanger two kinds of media can reach 1 DEG C, effectively can reclaim low temperature exhaust heat, material after sterilizing has reduced a lot in temperature after three grades of heat exchangers and secondary heat exchanger, utilize plate type heat exchanger to use up to recycle its waste heat to greatest extent and low temperature pan feeding is heated.
Further, described pre-heating system comprises the one-level plate type heat exchanger and secondary plate type heat exchanger that connect successively, after high-temperature sterilization, material is contrary with the throughput direction of low temperature pan feeding between one-level plate type heat exchanger, secondary plate type heat exchanger, effective increase heat exchanger effectiveness, after making sterilizing, the temperature of material reduces as far as possible, and the temperature of low temperature pan feeding improves as far as possible, effectively utilize waste heat, reduce sterilization treatment energy consumption.
Further, described pre-heating system enters pipeline place at low temperature pan feeding and is provided with triple valve I, and the pipeline that after sterilizing, material is transported to pre-heating system from heat exchange mechanism is provided with triple valve II, is connected between triple valve I with triple valve II by circulating line.The utility model utilizes triple valve I and triple valve II to come the break-make direction of control piper, when multifunction energy-saving high-temperature sterilization system worked well, circulating line between triple valve I and triple valve II is cut-off state, low temperature pan feeding is delivered in high-temperature sterilization mechanism according to the direction from pre-heating system to heat exchange mechanism and carries out high-temperature sterilization process, and the material after sterilizing simultaneously carries out filling after exporting along heat exchange mechanism to the direction of pre-heating system; When multifunction energy-saving high-temperature sterilization system needs to clear up, circulating line is communicated with pre-heating system by triple valve I, heat exchange mechanism is communicated with circulating line by triple valve II, whole multifunction energy-saving high-temperature sterilization system is made to become an inner loop loop, self-cleaning can be carried out easily, ensure the quality of sterilization treatment, to avoid on pipeline the impurity pollution materials such as breed bacteria.
Further, delivery pump is provided with between described pre-heating system and triple valve I, utilize delivery pump to provide power for the Flow of Goods and Materials of multifunction energy-saving high-temperature sterilization system, control the flow velocity of material, thus control the exchange rate of the material after low temperature pan feeding and sterilizing.
Further, be also provided with circulation barrel between described triple valve I and triple valve II to clear up for circulating.
Further, be provided with constant temperature zone between described high-temperature sterilization mechanism and heat exchange mechanism, lasting sterilizing guarantees that sterilizing is complete.
Further, described sterilizing tank body, high-temperature sterilization mechanism, heat exchange mechanism and pre-heating system all adopt stainless steel to make, and are convenient to clean, and ensure processing cleanliness factor, improve sterilization effect, ensure product quality.
Compared with prior art, the utility model advantage is:
The heat energy of the material after multifunction energy-saving high-temperature sterilization system recoveries described in the utility model utilizes sterilizing carries out preheating to the pan feeding of low temperature, significantly reduce the consumption of steam, water, improve the utilization ratio of the energy, reduce equipment power dissipation, energy-conserving and environment-protective, reduce production cost;
The utility model structure is simple, is easy to manufacture, and cost of manufacture is low, high financial profit.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
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.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
A kind of multifunction energy-saving high-temperature sterilization system disclosed in the utility model embodiment, recycle and reuse heat energy, reduces the consumption of steam, water, economize energy, reduces production cost.
As shown in Figure 1, a kind of multifunction energy-saving high-temperature sterilization system, comprise sterilizing tank body 1, sterilizing tank body 1 adopts thermal sterilization mode, high-temperature sterilization mechanism 2 and heat exchange mechanism 3 is provided with in sterilizing tank body 1, high-temperature sterilization mechanism 2 is provided with steam inlet 4, condensation-water drain 5 and pan feeding pipeline 6, material from pan feeding pipeline 6 enter be heated to 110 DEG C ~ 130 DEG C sterilizings by the high-temperature steam entered from steam inlet 4 is instantaneous in high-temperature sterilization mechanism 2 after export, constant temperature zone 17 is provided with between high-temperature sterilization mechanism 2 and heat exchange mechanism 3, maintain 6 seconds at constant temperature zone 17 and be delivered to heat exchange mechanism 3 after constant temperature, high-temperature sterilization mechanism 2, one-level heat exchanger 8 and two-stage heat exchanger 9 adopt bushing type heat exchange structure, heat exchanging pipe is tortuous in sterilizing tank body 1, heat exchange mechanism 3 comprises the one-level heat exchanger 8 and two-stage heat exchanger 9 that connect successively, after high-temperature sterilization, material and low temperature pan feeding are at one-level heat exchanger 8, throughput direction between two-stage heat exchanger 9 is contrary, low temperature pan feeding carries out high-temperature sterilization process by the pan feeding pipeline 6 entering into high-temperature sterilization mechanism 2 after heating material after high-temperature sterilization.
Pre-heating system 7 is connected with outer also setting of sterilizing tank body 1, low temperature pan feeding is successively through pre-heating system 7, heat exchange mechanism 3, be delivered to high-temperature sterilization mechanism 2 again, after high-temperature sterilization, material is then successively by heat exchange mechanism 3, pre-heating system 7, after low temperature pan feeding and high-temperature sterilization material carry out step by step heat exchange make high-temperature sterilization after material lower the temperature, and preheating is carried out to low temperature pan feeding.Pre-heating system 7 adopts plate type heat exchanger, pre-heating system 7 comprises the one-level plate type heat exchanger 10 and secondary plate type heat exchanger 11 that connect successively, after high-temperature sterilization, material is contrary with the throughput direction of low temperature pan feeding between one-level plate type heat exchanger 10, secondary plate type heat exchanger 11, and the sterilizing material after final reduction temperature carries out filling again.
High-temperature material after sterilizing and low temperature pan feeding carry out multistage heat exchange can the heat energy of material after more effective recycling sterilizing, improve the utilization ratio of heat energy, make the temperature difference of material after low temperature pan feeding and sterilizing in the heat exchanger of every one-level less, reduce thermal (temperature difference) stress, improve heat exchanger effectiveness.
Pre-heating system 7 enters pipeline place at low temperature pan feeding and is provided with triple valve I12, the pipeline that after sterilizing, material is transported to pre-heating system 7 from heat exchange mechanism 3 is provided with triple valve II13, be connected by circulating line 14 between triple valve I12 with triple valve II13, be provided with delivery pump 15 between pre-heating system 7 and triple valve I12, between triple valve I12 and triple valve II13, be also provided with circulation barrel 16.The duty of disinfection system is controlled by triple valve I12 and triple valve II13, when disinfection system normally works, circulating line 14 not conducting, low temperature pan feeding is delivered in high-temperature sterilization mechanism according to the direction from pre-heating system to heat exchange mechanism and carries out high-temperature sterilization process, and the material after sterilizing carries out filling after exporting along heat exchange mechanism to the direction of pre-heating system, when needs need to carry out internal cleaning to disinfection system, low temperature pan feeding blocks by triple valve I, circulating line 14 is communicated with pre-heating system by triple valve I12, heat exchange mechanism is communicated with circulation pipe 14 road by triple valve II13, whole multifunction energy-saving high-temperature sterilization system is made to become an inner loop loop, material in circulation barrel 16 is transported in pre-heating system by delivery pump 15, flow through heat exchange mechanism again, then enter in high-temperature sterilization system, finally be back in circulation barrel 13 along heat exchange mechanism to the direction of pre-heating system again, self-cleaning can be carried out easily, ensure the quality of sterilization treatment, avoid the impurity pollution material such as breed bacteria on pipeline.
Sterilizing tank body 1, high-temperature sterilization mechanism 2, heat exchange mechanism 3 and pre-heating system 7 all adopt stainless steel to make, easy cleaning, ensure product processing quality.
Below be only preferred embodiment of the present utility model, it should be pointed out that above-mentioned preferred embodiment should not be considered as restriction of the present utility model, protection domain of the present utility model should be as the criterion with claim limited range.For those skilled in the art, not departing from spirit and scope of the present utility model, can also make some improvements and modifications, these improvements and modifications also should be considered as protection domain of the present utility model.
Claims (10)
1. a multifunction energy-saving high-temperature sterilization system, comprise sterilizing tank body (1), it is characterized in that, described sterilizing tank body (1) adopts thermal sterilization mode, high-temperature sterilization mechanism (2) and heat exchange mechanism (3) is provided with in sterilizing tank body (1), high-temperature sterilization mechanism (2) is provided with steam inlet (4), condensation-water drain (5) and pan feeding pipeline (6), material enters in high-temperature sterilization mechanism (2) from pan feeding pipeline (6) and exports heat exchange mechanism (3) to by after the instantaneous heat sterilization of high-temperature steam entered from steam inlet (4), also arrange outward at sterilizing tank body (1) and be connected with pre-heating system (7), low temperature pan feeding is successively through pre-heating system (7), heat exchange mechanism (3), be delivered to high-temperature sterilization mechanism (2) again, after high-temperature sterilization, material is then successively by heat exchange mechanism (3), pre-heating system (7), after low temperature pan feeding and high-temperature sterilization material carry out step by step heat exchange make high-temperature sterilization after material lower the temperature, and preheating is carried out to low temperature pan feeding.
2. multifunction energy-saving high-temperature sterilization system according to claim 1, it is characterized in that, described heat exchange mechanism (3) comprises the one-level heat exchanger (8) and two-stage heat exchanger (9) that connect successively, and after high-temperature sterilization, material is contrary with the throughput direction of low temperature pan feeding between one-level heat exchanger (8), two-stage heat exchanger (9).
3. multifunction energy-saving high-temperature sterilization system according to claim 2, it is characterized in that, described high-temperature sterilization mechanism (2), one-level heat exchanger (8) and two-stage heat exchanger (9) adopt bushing type heat exchange structure, and heat exchanging pipe is tortuous in sterilizing tank body (1).
4. multifunction energy-saving high-temperature sterilization system according to claim 1, is characterized in that, described pre-heating system (7) adopts plate type heat exchanger.
5. multifunction energy-saving high-temperature sterilization system according to claim 4, it is characterized in that, described pre-heating system (7) comprises the one-level plate type heat exchanger (10) and secondary plate type heat exchanger (11) that connect successively, and after high-temperature sterilization, material is contrary with the throughput direction of low temperature pan feeding between one-level plate type heat exchanger (10), secondary plate type heat exchanger (11).
6. multifunction energy-saving high-temperature sterilization system according to claim 1, it is characterized in that, described pre-heating system (7) enters pipeline place at low temperature pan feeding and is provided with triple valve I (12), the pipeline that after sterilizing, material is transported to pre-heating system (7) from heat exchange mechanism (3) is provided with triple valve II (13), is connected between triple valve I (12) with triple valve II (13) by circulating line (14).
7. multifunction energy-saving high-temperature sterilization system according to claim 6, is characterized in that, is provided with delivery pump (15) between described pre-heating system (7) and triple valve I (12).
8. multifunction energy-saving high-temperature sterilization system according to claim 7, is characterized in that, is also provided with circulation barrel (16) between described triple valve I (12) and triple valve II (13).
9. multifunction energy-saving high-temperature sterilization system according to claim 1, is characterized in that, is provided with constant temperature zone (17) between described high-temperature sterilization mechanism (2) and heat exchange mechanism (3).
10. multifunction energy-saving high-temperature sterilization system according to claim 1, it is characterized in that, described sterilizing tank body (1), high-temperature sterilization mechanism (2), heat exchange mechanism (3) and pre-heating system (7) all adopt stainless steel to make.
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| CN201520173464.2U CN204499329U (en) | 2015-03-25 | 2015-03-25 | A kind of multifunction energy-saving high-temperature sterilization system |
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| CN201520173464.2U CN204499329U (en) | 2015-03-25 | 2015-03-25 | A kind of multifunction energy-saving high-temperature sterilization system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104663882A (en) * | 2015-03-25 | 2015-06-03 | 成都巨龙生物科技有限公司 | Multifunctional energy-saving high-temperature sterilization system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104663882A (en) * | 2015-03-25 | 2015-06-03 | 成都巨龙生物科技有限公司 | Multifunctional energy-saving high-temperature sterilization system |
| CN104663882B (en) * | 2015-03-25 | 2017-11-24 | 成都巨龙生物科技股份有限公司 | A kind of multifunction energy-saving high-temperature sterilization system |
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Address after: 610012 Wenjiang, Chengdu District, Chengdu, Taiwan Science and Technology Industrial Development Zone West Patentee after: Chengdu Julong biological Polytron Technologies Inc Address before: 610041, Wenjiang District, Sichuan City, Chengdu province Chengdu Straits science and Technology Industrial Development Zone West Patentee before: Chengdu Julong Biology Technology Co., Ltd. |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Multifunctional energy-saving high-temperature sterilization system Effective date of registration: 20170301 Granted publication date: 20150729 Pledgee: Agricultural Bank of China Limited by Share Ltd Chengdu Wenjiang branch Pledgor: Chengdu Julong biological Polytron Technologies Inc Registration number: 2017510000013 |
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Granted publication date: 20150729 Termination date: 20180325 |
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