CN205773461U - A kind of saline treatment and sterilizing combination unit - Google Patents
A kind of saline treatment and sterilizing combination unit Download PDFInfo
- Publication number
- CN205773461U CN205773461U CN201520817561.0U CN201520817561U CN205773461U CN 205773461 U CN205773461 U CN 205773461U CN 201520817561 U CN201520817561 U CN 201520817561U CN 205773461 U CN205773461 U CN 205773461U
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- China
- Prior art keywords
- crystallizing evaporator
- steam
- boiler
- salting
- sterilizing
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
- Y02P60/85—Food storage or conservation, e.g. cooling or drying
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- Apparatus For Disinfection Or Sterilisation (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The open a kind of saline treatment of this utility model and sterilizing combination unit, including boiler, crystallizing evaporator and sterilization tank, steam (vapor) outlet on boiler is connected to crystallizing evaporator by pipeline I provides Boiler Steam to crystallizing evaporator, salting waste water waterwater entrance from crystallizing evaporator enters crystallizing evaporator and is crystallized by Boiler Steam heating evaporation, the magma outlet bottom crystallizing evaporator of the magma of crystallization is discharged, the indirect steam that the evaporation of salting waste water obtains is delivered to sterilization tank by the indirect steam outlet discharge at crystallizing evaporator top by pipeline II and carries out heat sterilization to salted.Saline treatment described in the utility model and sterilizing combination unit efficiently solve the process problem of salting waste water after salted cleaning, and effective use of energy sources, when salting waste water is crystallized produce indirect steam carry out again with, indirect steam is utilized to carry out sterilization treatment to salted, it is effectively improved energy utilization rate, reduce production cost, reach the purpose of energy-saving and emission-reduction.
Description
Technical field
This utility model relates to salted processing unit (plant), particularly relates to a kind of saline treatment and sterilizing combination unit.
Background technology
During processing is salted, includes and clean and the manufacturing procedure of sterilizing.Using clear water to be carried out the dish after salting, can produce the salting waste water that a large amount of salinity is high, the difficult treatment of salting waste water after cleaning, general small business is difficult to process, it will usually directly give Sewage Plant to process.Salted sterilizing would generally use pasteurization process, utilizes high-temperature steam to the salted heat sterilization that carries out, and the sterilization treatment time is longer.In traditional salted processing, salting waste water processes and salted sterilizing is all individually to carry out, and expends resource big, processes the time long, and cost is high, inefficiency.
Utility model content
The technical assignment of technical problem to be solved in the utility model and proposition is to improve prior art, a kind of saline treatment and sterilizing combination unit are provided, solve current technology medium salting dish processing medium salting waste water and process big with salted sterilizing consuming resource, the process time is long, cost is high, ineffective problem.
For solving above technical problem, the technical solution of the utility model is:
A kind of saline treatment and sterilizing combination unit, including boiler, crystallizing evaporator and sterilization tank, it is characterized in that, tap water inlets and steam (vapor) outlet it is provided with on described boiler, steam (vapor) outlet is connected to crystallizing evaporator by pipeline I provides Boiler Steam to crystallizing evaporator, waterwater entrance is set on crystallizing evaporator, salting waste water enters crystallizing evaporator from waterwater entrance and is crystallized by Boiler Steam heating evaporation, the magma outlet bottom crystallizing evaporator of the magma of crystallization is discharged, the indirect steam that the evaporation of salting waste water obtains is delivered to sterilization tank by the indirect steam outlet discharge at crystallizing evaporator top by pipeline II and carries out heat sterilization to salted.Saline treatment described in the utility model and sterilizing combination unit efficiently solve the process problem of salting waste water after salted cleaning, and effective use of energy sources, when salting waste water is crystallized produce indirect steam carry out again with, indirect steam is utilized to carry out sterilization treatment to salted, it is effectively improved energy utilization rate, reduce production cost, reach the purpose of energy-saving and emission-reduction.Saline treatment described in the utility model and sterilizing combination unit can carry out two kinds of operations within the same time, make boiler maximum resource utilization, improve time availability, thus improve production efficiency.
Further, tortuous steam pipe is set in described crystallizing evaporator, salting waste water enters in crystallizing evaporator from waterwater entrance and flows through between steam pipe, salting waste water and the Boiler Steam generation heat exchange being passed through in steam pipe, and the Boiler Steam of condensation is discharged from condensation-water drain.This utility model utilizes steam pipe to make Boiler Steam and salting waste water carry out heat exchange, and Boiler Steam can reclaim along steam pipe condensation, and make salting waste water be heated evaporate portion of water after carry out crystallization and obtain magma, it is simple to follow-up carry out salt recycling.
Further, it is additionally provided with defecator at the waterwater entrance of described crystallizing evaporator to be re-fed into after salting waste water filtering in crystallizing evaporator, defecator is utilized to be filtered by impurity, avoid impurity to accumulate in crystallizing evaporator and cause blocking, crystallizing evaporator blocking is difficult to clear up, waste time and energy, affect production efficiency, the magma obtained can also be avoided impure simultaneously.
Further, the steam (vapor) outlet of described boiler is connected to pipeline II also by bypass line, and is both provided with Valve controlling break-make on bypass line and pipeline II.This utility model utilizes bypass line and pipeline II to realize the function of flexible manufacturing procedure, and under normal conditions, bypass line is closed, and pipeline II is open-minded, and salting waste water carries out crystallization treatment in crystallizing evaporator, salted carries out sterilization treatment in sterilization tank；Bypass line is opened, and closes crystallizing evaporator, does not the most carry out saline treatment, and the Boiler Steam that boiler produces directly enters in pipeline II along bypass line, and final Boiler Steam is passed directly into sterilization tank and carries out heat sterilization process to salted；Bypass line is closed, and pipeline II closes, and does not the most carry out sterilization treatment, the saline treatment operation being the most only evaporated in crystallizer.Saline treatment described in the utility model and sterilizing combination unit motility are strong, and easy to use, freely adjustable one-tenth individually carries out salting waste water process or sterilizing.
Further, being equipped with uniform sterilizing pipeline bottom described sterilization tank, indirect steam is high to the salted heat sterilization that carries out, heat transference efficiency in being passed through sterilizing pipeline, while effective sterilizing, reduces energy consumption, reaches the purpose of energy-saving and emission-reduction.
Further, in described sterilization tank, it is provided with conveyer belt, reduces labor intensity, salted sent into and send sterilization tank by conveyer belt, easy to use, and ensure salted cleanliness factor, it is to avoid personnel's taking and placing cause polluting.
Further, described sterilization tank is provided with housing makes sterilization tank be in closed state holding temperature stabilization when sterilizing, it is to avoid excess calories scatters and disappears and do not reaches the effect killing antibacterial completely, improves heating efficiency.
Further, described boiler, crystallizing evaporator, sterilization tank and pipeline all uses rustless steel to make, and cleanliness factor is good, corrosion-resistant, it is to avoid equipment remaining bacteria pollutes finished product.
Compared with prior art, this utility model advantage is:
Saline treatment described in the utility model and sterilizing combination unit efficiently solve the process problem of salting waste water after salted cleaning, and effective use of energy sources, when salting waste water is crystallized produce indirect steam carry out again with, indirect steam is utilized to carry out sterilization treatment to salted, it is effectively improved energy utilization rate, reduce production cost, reach the purpose of energy-saving and emission-reduction；Saline treatment described in the utility model and sterilizing combination unit can carry out two kinds of operations within the same time, make boiler maximum resource utilization, improve time availability, thus improve production efficiency；Boiler blow-down water and indirect steam water condensed water may be recovered recycling, further up to the purpose of energy-saving and emission-reduction；Saline treatment described in the utility model and sterilizing combination unit can individually carry out sterilizing and waste water processes and carries out, it is possible to processing, easy to adjust, motility is strong simultaneously.
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 this utility model embodiment, the technical scheme in this utility model embodiment is clearly and completely described, it is clear that described embodiment is only a part of embodiment of this utility model rather than whole embodiments.Based on the embodiment in this utility model, the every other embodiment that those of ordinary skill in the art are obtained under not making creative work premise, broadly fall into the scope of this utility model protection.
A kind of saline treatment and sterilizing combination unit disclosed in this utility model embodiment, salting waste water is processed and two operation integrated treatments of sterilizing, it is effectively improved energy utilization rate, reduce power consumption, reach the purpose of energy-saving and emission-reduction, and freely adjustable one-tenth individually carries out salting waste water process or sterilizing, motility is strong, easy to use.
nullAs shown in Figure 1，A kind of saline treatment and sterilizing combination unit，Including boiler 1、Crystallizing evaporator 2 and sterilization tank 3，Boiler 1、Crystallizing evaporator 2、Sterilization tank 3 and the pipeline connected all use rustless steel to make，Holding equipment cleanliness factor，Avoid bacteria breed，Tap water inlets 4 and steam (vapor) outlet 5 it is provided with on boiler 1，Steam (vapor) outlet 5 is connected to crystallizing evaporator 2 by pipeline I6 provides Boiler Steam to crystallizing evaporator 2，Tortuous steam pipe 11 is set in crystallizing evaporator 2，Waterwater entrance 7 is set on crystallizing evaporator 2，Salting waste water enters in crystallizing evaporator 2 from waterwater entrance 7 and flows through between steam pipe 11，Salting waste water and the Boiler Steam generation heat exchange being passed through in steam pipe 11，The Boiler Steam of condensation is discharged from condensation-water drain，Salting waste water is crystallized by Boiler Steam heating evaporation，Magma outlet 8 discharge bottom crystallizing evaporator 2 of the magma of crystallization，The indirect steam that the evaporation of salting waste water obtains is delivered to sterilization tank 3 by indirect steam outlet 9 discharge at crystallizing evaporator 2 top by pipeline II10 and carries out heat sterilization to salted.
It is additionally provided with at the waterwater entrance 7 of crystallizing evaporator 2 after the impurity in salting waste water is filtered by defecator 12 and is re-fed in crystallizing evaporator 2, it is to avoid impurity is accumulated in crystallizing evaporator and caused blocking.
In the present embodiment, the steam (vapor) outlet of boiler 1 is connected to pipeline II10 also by bypass line 13, and is both provided with Valve controlling break-make on bypass line 13 and pipeline II10.The break-make utilizing bypass line 13 and pipeline II10 freely regulates treatment process flexibly.Bypass line 13 is closed, and pipeline II10 is open-minded, and crystallizing evaporator 2 normally works, and salting waste water processes and sterilization process is carried out simultaneously；Bypass line 13 is opened, and closes crystallizing evaporator 2, and pipeline II10 is open-minded, does not the most carry out salting waste water treatment process, and the Boiler Steam that boiler produces directly enters in pipeline II10 along bypass line 13, only carries out sterilization treatment operation；Bypass line 13 is closed, and pipeline II10 closes, and does not the most carry out sterilization treatment operation, only carries out salting waste water treatment process.
Uniform sterilizing pipeline 14 it is equipped with bottom sterilization tank 3, indirect steam carries out heat sterilization to salted in being passed through sterilizing pipeline 14, sterilizing efficiency is high, energy consumption is low, it is provided with conveyer belt 15 in sterilization tank 3 and carries salted, reducing personnel labor intensity, sterilization tank 3 is provided with housing makes sterilization tank 3 be in closed state holding temperature stabilization when sterilizing.
Utilize above-mentioned saline treatment and the saline treatment of sterilizing combination unit and sterilization process, process step and include:
A. burning in boiler prepares the Boiler Steam of high temperature；
B. the Boiler Steam that step A obtains is passed through salting waste water evaporating, concentrating and crystallizing in crystallizing evaporator 2 with salting waste water generation heat exchange, Boiler Steam loses heat condensation and obtains boiler blow-down water, the part that salting waste water evaporates after absorbing heat is indirect steam, the part of crystallization is magma, magma pumped；
C. step B obtains indirect steam and is passed through sterilization tank 3 and carries out heat sterilization to salted, and indirect steam loses heat condensation and obtains indirect steam condensed water.
And the indirect steam condensate water circulatory that the boiler blow-down water that step B obtains and step C obtain recycles in the boiler of step A and is fired, recycle water resource, reduce production cost, condensed water still has waste heat, boiler can be reduced and fire the heat needed for steam, reduce power consumption, energy-saving and emission-reduction.
Below it is only preferred implementation of the present utility model, it is noted that above-mentioned preferred implementation is not construed as restriction of the present utility model, and protection domain of the present utility model should be as the criterion with claim limited range.For those skilled in the art, without departing from spirit and scope of the present utility model, it is also possible to making some improvements and modifications, these improvements and modifications also should be regarded as protection domain of the present utility model.
Claims (8)
- null1. a saline treatment and sterilizing combination unit，Including boiler (1)、Crystallizing evaporator (2) and sterilization tank (3)，It is characterized in that，Tap water inlets (4) and steam (vapor) outlet (5) it is provided with on described boiler (1)，Steam (vapor) outlet (5) is connected to crystallizing evaporator (2) by pipeline I (6) provides Boiler Steam to crystallizing evaporator (2)，Waterwater entrance (7) is set on crystallizing evaporator (2)，Salting waste water enters crystallizing evaporator (2) from waterwater entrance (7) and is crystallized by Boiler Steam heating evaporation，The magma of crystallization magma outlet (8) from crystallizing evaporator (2) bottom is discharged，The indirect steam that the evaporation of salting waste water obtains is delivered to sterilization tank (3) by indirect steam outlet (9) discharge at crystallizing evaporator (2) top by pipeline II (10) and carries out heat sterilization to salted.
- Saline treatment the most according to claim 1 and sterilizing combination unit, it is characterized in that, tortuous steam pipe (11) is set in described crystallizing evaporator (2), salting waste water enters in crystallizing evaporator (2) from waterwater entrance (7) and flows through between steam pipe (11), salting waste water and the Boiler Steam generation heat exchange being passed through in steam pipe (11), the Boiler Steam of condensation is discharged from condensation-water drain.
- Saline treatment the most according to claim 2 and sterilizing combination unit, it is characterized in that, waterwater entrance (7) place of described crystallizing evaporator (2) is additionally provided with defecator (12) and will be re-fed into after salting waste water filtering in crystallizing evaporator (2).
- Saline treatment the most according to claim 1 and sterilizing combination unit, it is characterized in that, the steam (vapor) outlet (5) of described boiler (1) is connected to pipeline II (10) also by bypass line (13), and is both provided with Valve controlling break-make on bypass line (13) and pipeline II (10).
- Saline treatment the most according to claim 1 and sterilizing combination unit, it is characterized in that, described sterilization tank (3) bottom is equipped with uniform sterilizing pipeline (14), and indirect steam carries out heat sterilization to salted in being passed through sterilizing pipeline (14).
- Saline treatment the most according to claim 5 and sterilizing combination unit, it is characterised in that in described sterilization tank (3), be provided with conveyer belt (15).
- Saline treatment the most according to claim 6 and sterilizing combination unit, it is characterised in that described sterilization tank (3) is provided with housing makes sterilization tank (3) be in closed state when sterilizing.
- Saline treatment the most according to claim 7 and sterilizing combination unit, it is characterised in that described boiler (1), crystallizing evaporator (2), sterilization tank (3) and pipeline all use rustless steel to make.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520533006 | 2015-07-22 | ||
| CN2015205330065 | 2015-07-22 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205773461U true CN205773461U (en) | 2016-12-07 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520817561.0U Expired - Fee Related CN205773461U (en) | 2015-07-22 | 2015-10-21 | A kind of saline treatment and sterilizing combination unit |
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|---|---|
| CN (1) | CN205773461U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105174335A (en) * | 2015-07-22 | 2015-12-23 | 成都百味坊贸易有限公司 | Brine treatment and sterilization combined device and process |
-
2015
- 2015-10-21 CN CN201520817561.0U patent/CN205773461U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105174335A (en) * | 2015-07-22 | 2015-12-23 | 成都百味坊贸易有限公司 | Brine treatment and sterilization combined device and process |
| CN105174335B (en) * | 2015-07-22 | 2017-12-15 | 成都百味坊贸易有限公司 | A kind of saline treatment and sterilizing combination unit and technique |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161207 |
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| CF01 | Termination of patent right due to non-payment of annual fee |