CN209178023U - Development waste liquid low temperature distillation handles all-in-one machine - Google Patents
Development waste liquid low temperature distillation handles all-in-one machine Download PDFInfo
- Publication number
- CN209178023U CN209178023U CN201821841211.8U CN201821841211U CN209178023U CN 209178023 U CN209178023 U CN 209178023U CN 201821841211 U CN201821841211 U CN 201821841211U CN 209178023 U CN209178023 U CN 209178023U
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- China
- Prior art keywords
- low temperature
- temperature distillation
- bucket
- cooling
- steam pipe
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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- 238000005292 vacuum distillation Methods 0.000 title claims abstract description 58
- 239000007788 liquid Substances 0.000 title claims abstract description 22
- 239000002699 waste material Substances 0.000 title claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 43
- 238000001816 cooling Methods 0.000 claims abstract description 42
- 239000000463 material Substances 0.000 claims description 15
- 239000007789 gas Substances 0.000 claims description 11
- 238000002309 gasification Methods 0.000 claims description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 7
- 239000001301 oxygen Substances 0.000 claims description 7
- 229910052760 oxygen Inorganic materials 0.000 claims description 7
- 238000002640 oxygen therapy Methods 0.000 claims description 7
- 239000003507 refrigerant Substances 0.000 claims description 6
- 239000012530 fluid Substances 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 4
- 230000006835 compression Effects 0.000 claims description 3
- 238000007906 compression Methods 0.000 claims description 3
- 238000006213 oxygenation reaction Methods 0.000 claims description 3
- 238000005086 pumping Methods 0.000 claims description 3
- 238000004821 distillation Methods 0.000 claims 1
- 238000010025 steaming Methods 0.000 claims 1
- 238000004080 punching Methods 0.000 abstract description 7
- 238000004134 energy conservation Methods 0.000 abstract description 3
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 238000007639 printing Methods 0.000 description 9
- 238000005516 engineering process Methods 0.000 description 4
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- 239000013043 chemical agent Substances 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000012153 distilled water Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 235000015114 espresso Nutrition 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 230000004913 activation Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model provides a kind of development waste liquid low temperature distillation processing all-in-one machine, including body, it further includes set on the intracorporal low temperature distillation bucket of the machine, cooling bucket, heat pump system and the vacuum evacuation device for controlling low temperature distillation bucket vacuum.Feed inlet, low temperature distillation bucket bottom are equipped at the top of low temperature distillation bucket equipped with vacuum tube, low temperature distillation bucket is connected by vacuum tube with the vacuum evacuation device.Steam pipe is additionally provided in low temperature distillation bucket, steam pipe is located at low temperature distillation bucket top, and the position that cooling bucket corresponds to steam pipe is equipped with input end and the input end is connected with steam pipe.Heat pump system includes condenser, evaporator and compressor, and condenser, evaporator and compressor form closed cycle system by placed in series.The utility model can effectively reduce the consumption of the energy and the generation of punching water, reduce production cost, and energy conservation and environmental protection, and treated, and water can be recycled repeatedly, be suitble to large-scale popularization and application.
Description
Technical field
The utility model relates to purification technology field, especially a kind of development waste liquid low temperature distillation handles all-in-one machine.
Background technique
In printing industry, plate-making developing process is most common technology in printing industry now, is being developed every time
Meeting residual fraction developer solution and impurity on rear printing plate are finished printing, these residues can destroy picture and text the printing effect of part
Fruit causes printing plate press resistance rate to decline, influences printing product quality and production efficiency.So development needs after finishing printing every time
It to use a large amount of clean water to be rinsed printing plate, to remove the various residues on plate, can generate so a large amount of
Punching water, increase the production cost of enterprise.Secondly, the punching water after rushing version contains the developer solution ingredient of high concentration, if directly
Run in and put, serious pollution can be not only caused to environment, can also waste a large amount of water resource.Also, conventional purification apparatus is most
Cooling using electric heating and water-cooling pattern, energy consumption is big, and heating and cooling effect are bad.Therefore, it is necessary to one kind can
Enough satisfactions rush version demand, and can recycle and rush version water purifying means.
Summary of the invention
The purpose of the utility model is to provide the development waste liquid low temperature distillations that one kind can effectively overcome the above problem to occur
All-in-one machine is handled, it not only can be with distil(l) punching water, but also the punching water after distil(l) is Ke Xunhuanliyong.
Purpose of the utility model is realized as follows: a kind of development waste liquid low temperature distillation handles all-in-one machine, including body,
It further includes set on the intracorporal low temperature distillation bucket of the machine, cooling bucket, heat pump system and the pumping for controlling low temperature distillation bucket vacuum
Vacuum plant；Feed inlet, low temperature distillation bucket bottom are equipped at the top of the low temperature distillation bucket equipped with vacuum tube, low temperature distillation bucket passes through
The vacuum tube is connected with the vacuum evacuation device；Steam pipe is equipped in low temperature distillation bucket, steam pipe is located at low temperature distillation bucket
Top, the position that the cooling bucket corresponds to steam pipe is equipped with input end and the input end is connected with steam pipe；The heat pump system
System includes condenser, evaporator and compressor, and the condenser, evaporator and compressor form closed circulation by placed in series
System, wherein condenser is set in low temperature distillation bucket, for heating to the material in low temperature distillation bucket, and evaporator is set to
Enter the vapor in cooling bucket in cooling bucket, for cooling through steam pipe.
In above structure, it is provided with fluid reservoir and expansion valve on the pipeline that the condenser is connect with evaporator one end, steams
Gas-liquid separator is provided on the pipeline that hair device is connect with the compressor other end；Low-temperature low-pressure refrigerant in evaporator is from outside
It is inhaled into compressor after endothermic gasification in air, the refrigerant compression after gasification is sent by compressor at high temperature and high pressure gas
In condenser, high temperature and high pressure gas heats the material in low temperature distillation bucket in condenser, its ebullition, gasification is made to form water
Steam, vapor enter in cooling bucket through steam pipe；High temperature and high pressure gas cooling condensation after being heated to material in condenser
It at highly pressurised liquid, is flowed into evaporator after expanded valve throttling cooling, evaporator carries out the vapor entered in cooling bucket cold
But.
In above structure, the cooling bucket bottom is equipped with drainpipe, is equipped with drain valve in the drainpipe.
In above structure, it further includes a water tank, and the water tank is set to cooling bucket side and the water tank is connected with drainpipe
It is logical.
In above structure, the water tank bottom is connected with oxygen cathete, and oxygen therapy pump, the oxygen therapy are equipped on the oxygen cathete
Pump is for being the water oxygenation in water tank.
In above structure, the vacuum tube that the low temperature distillation bucket is connect with vacuum evacuation device is equipped with solenoid valve, the electricity
Magnet valve is closed for controlling the logical of pipeline.
The utility model first vacuumizes low temperature distillation bucket, then will heat to material, and material is 30 under negative pressure state
Degree left and right ebullition, gasification and can form vapor, and vapor is converted to water after entering cooling bucket condensation；The product uses low temperature
The principle of vacuum distillation gets rid of Conventional espresso and adds the traditional mode of chemical agent filters pressing, also, the water by being distilled to recover can
It recycles again.Wherein, the distilled water that 70%-90% reaches discharge standard can be generated after purifying to material filtering, it can be again
It is recycled, the concentrate storage of remaining 10-30% waits the transfer of third party's dangerous waste, also, low temperature distillation technology will not produce
The secondary pollutions such as raw exhaust gas.The utility model can effectively reduce the consumption of the energy and the generation of punching water, reduction are produced into
This, and energy conservation and environmental protection, treated, and water can be recycled repeatedly, be suitble to large-scale popularization and application.
Detailed description of the invention
Fig. 1 is the utility model overall structure diagram；
Fig. 2 is the schematic diagram of the utility model heat pump system.
In figure: low temperature distillation bucket 1, cooling bucket 2, heat pump system 3, vacuum evacuation device 4, water tank 5, oxygen cathete 6, oxygen therapy pump 7,
Feed inlet 10, vacuum tube 11, steam pipe 12, input end 20, drainpipe 21, condenser 30, evaporator 31, compressor 32, liquid storage
Tank 33, expansion valve 34, gas-liquid separator 35.
Specific embodiment
The utility model is described in further detail with reference to the accompanying drawing
As depicted in figs. 1 and 2, the utility model discloses a kind of development waste liquid low temperature distillation processing all-in-one machine, including body,
It further includes set on the intracorporal low temperature distillation bucket 1 of machine, cooling bucket 2, heat pump system 3 and the pumping for controlling 1 vacuum of low temperature distillation bucket
Vacuum plant 4.Specifically, feed inlet 10 is equipped at the top of low temperature distillation bucket 1,1 bottom of low temperature distillation bucket is equipped with vacuum tube 11, low temperature
Distillation bucket 1 is connected by vacuum tube 11 with vacuum evacuation device 4.It is additionally provided with steam pipe 12 in low temperature distillation bucket 1, steam pipe 12
In 1 top of low temperature distillation bucket.The position of the cooling corresponding steam pipe 12 of bucket 2 is equipped with input end 20, the input end 20 and steam pipe 11
It is connected, and steam pipe 11 is equipped with solenoid valve, solenoid valve is closed for controlling the logical of steam pipe 11.
Further, as shown in Figure 2, heat pump system 3 includes condenser 30, evaporator 31 and compressor 32, condenser
30, evaporator 31 and compressor 32 form closed cycle system by placed in series, wherein condenser 30 is set to low temperature distillation bucket
In 1, for being heated to the material in low temperature distillation bucket 1, evaporator 31 is set in cooling bucket 2, for cooling through steam pipe
12 vapor entered in cooling bucket 2 are cooled down.In more detail, it is set on the pipeline that condenser 30 is connect with 31 one end of evaporator
It is equipped with fluid reservoir 33 and expansion valve 34, is provided with gas-liquid separator on the pipeline that evaporator 31 is connect with 32 other end of compressor
35.For low-temperature low-pressure refrigerant in evaporator 31 from being inhaled into compressor 32 after endothermic gasification in cooling bucket 2, compressor will
Refrigerant compression after gasification is sent into condenser 30 at high temperature and high pressure gas, and high temperature and high pressure gas steams low temperature in condenser 30
The material evaporated in bucket 1 is heated, its ebullition, gasification is made to form vapor；High temperature and high pressure gas in condenser 30 is to material
Cooling condenses into highly pressurised liquid and flows into fluid reservoir 33 after heating, the expanded throttling of valve 34 cooling of the highly pressurised liquid in fluid reservoir 33
It flows into evaporator 31 afterwards, evaporator 31, which carries out cooling to the vapor entered in cooling bucket 2 again, makes its vapor be condensed into water
And it collects in water tank 5.Since above-mentioned heat pump system is the prior art, does not just tire out one by one chat here.
Preferably, cooling 2 bottom of bucket sets drainpipe 21, is equipped with drain valve (not shown) in drainpipe 21.
Preferably, it further includes a water tank 5, and water tank 5 is set to cooling 2 side of bucket and the water tank 5 is connected with drainpipe 21
Logical, condensed water can be collected in water tank 5 through drainpipe 21.Also, 5 bottom of water tank is connected with oxygen cathete 6, on oxygen cathete 6
Oxygen therapy pump 7 is installed, oxygen therapy pump 7 makes its activation be recycled for carrying out oxygenation for the water in water tank 5.
Preferably, the vacuum tube 11 that low temperature distillation bucket 1 is connect with vacuum evacuation device 4 is equipped with solenoid valve (not shown), electricity
Magnet valve is closed for controlling the logical of pipeline.
The utility model first vacuumizes low temperature distillation bucket, then will heat to material, and material is 30 under negative pressure state
Degree left and right ebullition, gasification and can form vapor, and vapor is converted to water after entering cooling bucket condensation；The product uses low temperature
The principle of vacuum distillation gets rid of Conventional espresso and adds the traditional mode of chemical agent filters pressing, also, the water by being distilled to recover can
It recycles again.Wherein, the distilled water that 70%-90% reaches discharge standard can be generated after purifying to material filtering, it can be again
It is recycled, the concentrate storage of remaining 10-30% waits the transfer of third party's dangerous waste, also, low temperature distillation technology will not produce
The secondary pollutions such as raw exhaust gas.The utility model can effectively reduce the consumption of the energy and the generation of punching water, reduction are produced into
This, and energy conservation and environmental protection, treated, and water can be recycled repeatedly, be suitble to large-scale popularization and application.
The foregoing is merely this patent preferred embodiments, not limit this patent range, all using specification and attached
Equivalent structure or equivalent flow shift made by figure content is directly or indirectly used in other relevant technical fields, belongs to
The scope of this patent.
Claims (6)
1. a kind of development waste liquid low temperature distillation handles all-in-one machine, including body, it is characterised in that: it further includes being set to the body
Interior low temperature distillation bucket, cooling bucket, heat pump system and the vacuum evacuation device for controlling low temperature distillation bucket vacuum；The low temperature distillation
Feed inlet, low temperature distillation bucket bottom are equipped at the top of bucket equipped with vacuum tube, low temperature distillation bucket is true by the vacuum tube and the pumping
Empty device is connected；Steam pipe is additionally provided in low temperature distillation bucket, steam pipe is located at low temperature distillation bucket top, and the cooling bucket is corresponding
The position of steam pipe is equipped with input end and the input end is connected with steam pipe；The heat pump system includes condenser, evaporator
And compressor, the condenser, evaporator and compressor form closed cycle system by placed in series, wherein condenser is set
In in low temperature distillation bucket, for being heated to the material in low temperature distillation bucket, evaporator is set in cooling bucket, for cooling warp
Steam pipe enters the vapor in cooling bucket.
2. development waste liquid low temperature distillation according to claim 1 handles all-in-one machine, it is characterised in that: the condenser and steaming
It is provided with fluid reservoir and expansion valve on the pipeline of hair device one end connection, is arranged on the pipeline that evaporator is connect with the compressor other end
There is gas-liquid separator；Low-temperature low-pressure refrigerant in evaporator is inhaled into compressor after endothermic gasification in outside air,
Refrigerant compression after gasification is sent into condenser by compressor at high temperature and high pressure gas, and high temperature and high pressure gas is to low in condenser
Material in temperature distillation bucket is heated, and so that its ebullition, gasification is formed vapor, vapor enters in cooling bucket through steam pipe；It is cold
High temperature and high pressure gas in condenser is cooling after heating to material to condense into highly pressurised liquid, flows into and steams after expanded valve throttling cooling
It sends out in device, evaporator cools down the vapor entered in cooling bucket.
3. development waste liquid low temperature distillation according to claim 1 handles all-in-one machine, it is characterised in that: the cooling bucket bottom
Equipped with drainpipe, drain valve is equipped in the drainpipe.
4. a kind of development waste liquid low temperature distillation according to claim 3 handles all-in-one machine, it is characterised in that: it further includes one
Water tank, the water tank is set to cooling bucket side and the water tank is connected with drainpipe.
5. development waste liquid low temperature distillation according to claim 4 handles all-in-one machine, it is characterised in that: the water tank bottom connects
It is connected to oxygen cathete, oxygen therapy pump is installed on the oxygen cathete, the oxygen therapy pump is used for as the water oxygenation in water tank.
6. development waste liquid low temperature distillation according to claim 1 handles all-in-one machine, it is characterised in that: the low temperature distillation bucket
The vacuum tube connecting with vacuum evacuation device is equipped with solenoid valve, and the solenoid valve is closed for controlling the logical of pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821841211.8U CN209178023U (en) | 2018-11-09 | 2018-11-09 | Development waste liquid low temperature distillation handles all-in-one machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821841211.8U CN209178023U (en) | 2018-11-09 | 2018-11-09 | Development waste liquid low temperature distillation handles all-in-one machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209178023U true CN209178023U (en) | 2019-07-30 |
Family
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821841211.8U Expired - Fee Related CN209178023U (en) | 2018-11-09 | 2018-11-09 | Development waste liquid low temperature distillation handles all-in-one machine |
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| CN (1) | CN209178023U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112415846A (en) * | 2020-11-30 | 2021-02-26 | 薛海龙 | Photographic fixing solution preparation device for developing of imaging department |
-
2018
- 2018-11-09 CN CN201821841211.8U patent/CN209178023U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112415846A (en) * | 2020-11-30 | 2021-02-26 | 薛海龙 | Photographic fixing solution preparation device for developing of imaging department |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190730 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |