CN101954196A - Distillation recovery system - Google Patents
Distillation recovery system Download PDFInfo
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- CN101954196A CN101954196A CN 201010268288 CN201010268288A CN101954196A CN 101954196 A CN101954196 A CN 101954196A CN 201010268288 CN201010268288 CN 201010268288 CN 201010268288 A CN201010268288 A CN 201010268288A CN 101954196 A CN101954196 A CN 101954196A
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- distillation
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- recovery system
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Abstract
The invention discloses a distillation recovery system and is applied to the technical field of industrial cleaners. The distillation recovery system comprises a distillation tank, a carbon dioxide compressor and a carbon dioxide pressure reducer, wherein a heating loop is formed by a heater and the distillation tank; a cooling loop is formed by a cooler, a condensate tank and a circulating tank respectively; a carbon dioxide refrigerating and heating system is formed by the carbon dioxide compressor, the heater, the carbon dioxide pressure reducer and the cooler; and the distillation tank, the condensate tank and the circulating tank are sequentially connected through pipelines. The distillation recovery system has the advantages of simple structure, high energy utilization rate and convenient cleaning and maintenance.
Description
Technical field
The present invention relates to industrial cleaning machine technical field, relate in particular to a kind of distillation recovery system.
Background technology
Used cleaning agent in the industry cleaning machine contaminatedly gradually in cleaning process is lost cleaning capacity for the cleaning agent waste liquid.If these cleaning agent waste liquids are directly outwelled, not only increase and clean cost, and can pollute environment.Therefore, need recycle processing to the cleaning agent waste liquid.
Usually adopt the distillation recovery system that the cleaning agent waste liquid is recycled processing, earlier the distillation of cleaning agent waste liquid is obtained cleaning agent volatilization composition, and then the cleaning agent composition condensation of volatilizing is obtained pure cleaning agent.In the distillation recovery system of prior art, needing external heat source usually provides heat to make low-volatile cleaning agent composition in the cleaning agent waste liquid in the vacuum state evaporation and taken away in the cleaning agent waste liquid of heating in the distillation tank; Simultaneously, need establish external source in addition is condensed into the cleaning agent composition extracted out and becomes pure cleaning agent and flow out at condensate tank(trap).This not only needs a special heating so that distillation tank is heated with regard to making, and needs a special refrigeration system to be used for the condensation of cleaning agent volatilization composition so that cold to be provided in addition.Therefore, there is baroque defective in existing distillation recovery system.
And, because present heat, refrigeration system all is to adopt electric energy to carry out work, and we know that evaporation 1 premium on currency needs about 540 caloric heats, and 1 kilowatt of eletctric energy (KWE) can be converted into about 860 caloric heats, even under the situation that energy is very changed, 1 kilowatt energy approximately can only make 1.59 liters water evaporation.That is to say and present distillation recovery system directly utilize electric energy to heat, freeze to exist energy consumption height, defective that capacity usage ratio is low, the enterprise that this and current social are advocated to need energy-saving and emission-reduction to require be unfavorable.
In addition, the distillation tank that uses in the present distillation recovery system, its structure is that coil pipe is set in groove.During heating, be connected with the heating agent conduction oil in the coil pipe cleaning agent waste liquid is heated.Because coil pipe produces very high temperature after heating, the impurity in the cleaning agent waste liquid is easily adsorbed in its vicinity, just make the coil pipe fouling for a long time.Coil pipe after the fouling the heating distillate the time, be prone to the heating uneven situation.Therefore, this regularly cleans distillation tank and coil pipe with regard to needs, because coil pipe is complicated helical structure, directly cleaning can't be carried out, and coil pipe must be dismantled during cleaning.Therefore, there is the defective of cleaning difficulty in existing distillation tank.
Summary of the invention
First technical problem to be solved by this invention provide a kind of simple in structure, capacity usage ratio is high, the distillation recovery system of saving the energy, to overcome the deficiency that prior art exists.
In order to solve the problems of the technologies described above, the present invention adopts following technical scheme:
A kind of distillation recovery system, comprise distillation tank, carbon dioxide compression device and carbon dioxide pressure reducer, heater and distillation tank form heating circuit, cooler forms cooling circuit with condensate tank(trap) and circulating slot respectively, carbon dioxide compression device, heater, carbon dioxide pressure reducer and cooler form the carbon dioxide refrigeration heating, and described distillation tank, condensate tank(trap), circulating slot are linked in sequence by pipeline.In the present invention, can provide thermal source and low-temperature receiver simultaneously owing to only relate to distillation tank, condensate tank(trap), circulating slot, carbon dioxide refrigeration heating and carbon dioxide refrigeration heating in the whole distillation recovery system, therefore, the present invention has advantage of simple structure.
In addition, in the carbon dioxide refrigeration heating, on the one hand send heater to, realize heating distillation tank with producing heat in the carbon dioxide compression device carbon dioxide being compressed; On the other hand, pass to cooler and think that condensate tank(trap), circulating slot provide cold with in the carbon dioxide pressure reducer carbon dioxide of high pressure being discharged to obtain cold, same system can heat and can freeze.And this system 1 kilowatt of eletctric energy (KWE) approximately can produce 4300 caloric heats, and its efficient is about 5 times of the prior art, and therefore, the present invention also has the capacity usage ratio height, the advantage that can economize on resources.
Second technical problem to be solved by this invention is that distillation tank can convenient for cleaningly be safeguarded, for this reason, distillation tank of the present invention comprises cell body and is arranged at groove lid on the cell body that heating interlayer and described cell body bottom interior wall that described cell body bottom has hollow are pasted with one deck high-temperature resistant membrane.
In distillation tank distillation cleaning agent waste liquid process, bubble can be produced, and impurity can be mingled with in the bubble, in order to access pure cleaning agent volatilization composition, the present invention is in further improving, and described groove lid below is provided with an electromagnetic shaker.This electromagnetic shaker can be shatter with bubble, sneaks into down-stream in the bubble thereby avoided impurity to be mixed in, thereby avoiding influencing reclaims the pure of the cleaning agent that obtains.The heating-up temperature of heater of the present invention is 90-100 ℃; The chilling temperature of cooler is 15-20 ℃.
For the cleaning agent condensate liquid in the condensate tank(trap) successfully being transferred to circulating slot, also include circulating pump and threeway, described circulating slot and circulating pump, threeway form closed circuit, described threeway one end communication loop pump, one end communication loop groove, the other end is communicated with condensate tank(trap).Abundant for the condensation that further guarantees cleaning agent volatilization composition, between described condensate tank(trap) and distillation tank, also be provided with heat exchanger, described cooler and condensate tank(trap), heat exchanger also form a cooling circuit.
Therefore, in sum, that distillation recovery system of the present invention has is simple in structure, energy utilizes high, cleaning advantage easily.
Description of drawings
Fig. 1 is a system schematic of the present invention;
Fig. 2 is a distillation tank system schematic of the present invention.
Among the figure: 100-cleaning agent waste liquid inlet 200-filter 300-distillation tank 301-cell body 302-groove lid 303-carrier pipe 304-hollow heating interlayer 305-high-temperature resistant membrane 306-electromagnetic shaker 400-heat exchanger 500-condensate tank(trap) 600-circulating slot 601-circulating pump 602-threeway 700-outlet 800-carbon dioxide refrigeration heating 801-cooler 802-heater 803-compressor reducer 804-pressure reducer 900-heat heat exchanger.
The specific embodiment
Below in conjunction with specific embodiment the present invention is further described:
See also Fig. 1, it is a system schematic of the present invention, comprises filter 200, distillation tank 300, heat exchanger 400, condensate tank(trap) 500, circulating slot 600 and carbon dioxide refrigeration heating 800.
Axial-flow pump sucks the cleaning agent waste liquid from the cleaning agent waste liquid inlet 100 that distills the recovery system bottom, be mixed with impurity such as impurity, dirt, iron powder usually owing in the cleaning agent waste liquid, the cleaning agent waste liquid is filtered to be delivered to through filter 200 reach distillation tank 300.
See also Fig. 2, distillation tank 300 comprises cell body 301, groove lid 302, and groove lid 302 covers on cell body 301, and makes whole distillation tank 300 inside be in sealing by sealing means.Hollow heating interlayer 304 is arranged in cell body 301 bottoms, and the inside is connected with the heating agent conduction oil.Be connected in carrier pipe 303 1 ends on the groove lid 302, carrier pipe 303 other ends are connected with condensate tank(trap) 500.
Cleaning agent waste liquid in cell body 301 the insides through the heating agent heat-conducting oil heating of 304 li of empty heating interlayers, makes the volatilization of cleaning agent composition and passes through carrier pipe 303 to condensate tank(trap) 500 conveyings.
Groove covers 302 belows and is provided with an electromagnetic shaker 306.Electromagnetic shaker 306 can be shatter with bubble, sneaks into down-stream in the bubble thereby avoided impurity to be mixed in, thereby avoiding influencing reclaims the pure of the cleaning agent that obtains.
Distillation tank 300 also is included in cell body 301 bottom interior wall and is pasted with one deck high-temperature resistant membrane 305, and high-temperature resistant membrane 305 is high temperature resistant about the 150 ℃ resin films of energy.When distillation tank 300 is carried out the cleaning of inner dirt, only need high-temperature resistant membrane 305 taken off from cell body 301 bottoms get final product, need not to adopt in addition again cleaning agent or water cleaning cell body inside, economize on resources, reduce pollution, clear up very convenient.
See also Fig. 1, carbon dioxide refrigeration heating 800 is formed by carbon dioxide compression device 803, heater 802, carbon dioxide pressure reducer 804 and cooler 801.
Distillation tank 300 forms heating circuit through heat release with heat exchanger 900 and heater 802.802 pairs of heating agent heat-conducting oil heating of heater, this gives distillation tank 300 the insides cleaning agent waste liquid heating to be processed indirectly.
In distillation tank 300, the low volatilization composition in the cleaning agent waste liquid is heated volatilization and is detached distillation tank 300, and the cleaning agent volatilization composition of being taken away arrives condensate tank(trap) 500 through heat exchanger 400.
Condensate tank(trap) 500 and circulating slot 600 rely on cooler 801 coolings, and condensate tank(trap) 500 and circulating slot 600 form cooling circuit with cooler 801 respectively.
In condensate tank(trap) 500, cleaning agent volatilization composition is condensed into the cleaning agent condensate liquid, and condensate liquid is through circulating slot 600 and export 700 outflow systems.
For the cleaning agent condensate liquid in the condensate tank(trap) 500 successfully being transferred to circulating slot 600, also include circulating pump 601 and threeway 602, described circulating slot 600 and circulating pump 601, threeway 602 form closed circuit, described threeway 602 1 end communication loop pumps 601, one end communication loop groove 600, the other end is communicated with condensate tank(trap) 500.
Abundant for the condensation that further guarantees cleaning agent volatilization composition, between condensate tank(trap) 500 and distillation tank 300, also be provided with heat exchanger 400, cooler 801 and condensate tank(trap) 500, heat exchanger 400 also form a cooling circuit.
In the carbon dioxide refrigeration heating 800, on the one hand send heater 802 to, realize heating distillation tank 300 with producing heat in the carbon dioxide compression device 803 carbon dioxide being compressed; On the other hand, pass to cooler 801 and think that condensate tank(trap) 500, circulating slot 600 provide cold with in the carbon dioxide pressure reducer 804 carbon dioxide of high pressure being discharged to obtain cold, same system can heat and can freeze.And this system 1 kilowatt of eletctric energy (KWE) approximately can produce 4300 caloric heats, and its efficient is about 5 times of the prior art, and therefore, the present invention also has the capacity usage ratio height, the advantage that can economize on resources.
Can provide thermal source and low-temperature receiver, advantage of simple structure simultaneously owing to only relate to distillation tank 300, condensate tank(trap) 500, circulating slot 600, carbon dioxide refrigeration heating 800 and carbon dioxide refrigeration heating 800 in the whole distillation recovery system.
This makes is not needing to be provided with under the situation of independent external heat source and external source, and the recycling by carbon dioxide refrigeration heating 800 realization cleaning agent waste liquids not only simplifies the structure, and reaches the environmental protection purpose of energy-saving and emission-reduction.
Claims (7)
1. one kind is distilled recovery system, it is characterized in that: comprise distillation tank, carbon dioxide compression device and carbon dioxide pressure reducer, heater and distillation tank form heating circuit, cooler forms cooling circuit with condensate tank(trap) and circulating slot respectively, carbon dioxide compression device, heater, carbon dioxide pressure reducer and cooler form the carbon dioxide refrigeration heating, and described distillation tank, condensate tank(trap), circulating slot are linked in sequence by pipeline.
2. distillation recovery system according to claim 1 is characterized in that: described distillation tank comprises cell body and is arranged at groove lid on the cell body that heating interlayer and described cell body bottom interior wall that described cell body bottom has hollow are pasted with one deck high-temperature resistant membrane.
3. distillation recovery system according to claim 2 is characterized in that: described groove lid below is provided with an electromagnetic shaker.
4. distillation recovery system according to claim 1 is characterized in that: the heating-up temperature of described heater is 90-100 ℃.
5. distillation recovery system according to claim 1 is characterized in that: the chilling temperature of described cooler is 15-20 ℃.
6. distillation recovery system according to claim 1, it is characterized in that: also include circulating pump and threeway, described circulating slot and circulating pump, threeway form closed circuit, described threeway one end communication loop pump, one end communication loop groove, the other end is communicated with condensate tank(trap).
7. distillation recovery system according to claim 1 is characterized in that: also be provided with heat exchanger between described condensate tank(trap) and the distillation tank, described cooler and condensate tank(trap), heat exchanger also form a cooling circuit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010102682882A CN101954196B (en) | 2010-08-27 | 2010-08-27 | Distillation recovery system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN2010102682882A CN101954196B (en) | 2010-08-27 | 2010-08-27 | Distillation recovery system |
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| CN101954196A true CN101954196A (en) | 2011-01-26 |
| CN101954196B CN101954196B (en) | 2012-05-23 |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103288154A (en) * | 2013-05-15 | 2013-09-11 | 中色科技股份有限公司 | Device and method for recovering metal material surface cleaning agent |
| CN103520942A (en) * | 2013-10-12 | 2014-01-22 | 象山医疗精密仪器有限公司 | Medicament concentration evaporation apparatus |
| CN108096866A (en) * | 2018-01-31 | 2018-06-01 | 深圳市鑫承诺环保产业股份有限公司 | Hydrocarbon solution recovery device |
| CN109621472A (en) * | 2018-12-27 | 2019-04-16 | 昆山城东化工有限公司 | A kind of multistage cooling recovery system for organic solvent |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH09290101A (en) * | 1996-04-24 | 1997-11-11 | Asahi Seimitsu Kk | Cleaning liquid recycling device |
| CN1846827A (en) * | 2005-04-15 | 2006-10-18 | 上海科伟达超声波科技有限公司 | Vacuum distillation process for recovering and regenerating washing liquid |
| CN101002991A (en) * | 2006-01-20 | 2007-07-25 | 梁诗文 | Closing circulation type system for recovering solvent |
| CN201216885Y (en) * | 2008-07-08 | 2009-04-08 | 江苏卡特石油新能源有限公司 | Methanol recycling apparatus |
| CN201551863U (en) * | 2009-12-03 | 2010-08-18 | 立邦涂料（中国）有限公司 | Solvent recovery system and reactor thereof |
-
2010
- 2010-08-27 CN CN2010102682882A patent/CN101954196B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH09290101A (en) * | 1996-04-24 | 1997-11-11 | Asahi Seimitsu Kk | Cleaning liquid recycling device |
| CN1846827A (en) * | 2005-04-15 | 2006-10-18 | 上海科伟达超声波科技有限公司 | Vacuum distillation process for recovering and regenerating washing liquid |
| CN101002991A (en) * | 2006-01-20 | 2007-07-25 | 梁诗文 | Closing circulation type system for recovering solvent |
| CN201216885Y (en) * | 2008-07-08 | 2009-04-08 | 江苏卡特石油新能源有限公司 | Methanol recycling apparatus |
| CN201551863U (en) * | 2009-12-03 | 2010-08-18 | 立邦涂料（中国）有限公司 | Solvent recovery system and reactor thereof |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103288154A (en) * | 2013-05-15 | 2013-09-11 | 中色科技股份有限公司 | Device and method for recovering metal material surface cleaning agent |
| CN103288154B (en) * | 2013-05-15 | 2015-04-08 | 中色科技股份有限公司 | Device and method for recovering metal material surface cleaning agent |
| CN103520942A (en) * | 2013-10-12 | 2014-01-22 | 象山医疗精密仪器有限公司 | Medicament concentration evaporation apparatus |
| CN103520942B (en) * | 2013-10-12 | 2015-08-12 | 象山医疗精密仪器有限公司 | Medicine concentration and evaporation device |
| CN108096866A (en) * | 2018-01-31 | 2018-06-01 | 深圳市鑫承诺环保产业股份有限公司 | Hydrocarbon solution recovery device |
| CN109621472A (en) * | 2018-12-27 | 2019-04-16 | 昆山城东化工有限公司 | A kind of multistage cooling recovery system for organic solvent |
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| Publication number | Publication date |
|---|---|
| CN101954196B (en) | 2012-05-23 |
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