CN203598663U - Hydrocarbon solution recovery system - Google Patents
Hydrocarbon solution recovery system Download PDFInfo
- Publication number
- CN203598663U CN203598663U CN201320810692.7U CN201320810692U CN203598663U CN 203598663 U CN203598663 U CN 203598663U CN 201320810692 U CN201320810692 U CN 201320810692U CN 203598663 U CN203598663 U CN 203598663U
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- China
- Prior art keywords
- air
- hydrocarbon solution
- groove
- blast pipe
- recovery system
- 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 - Lifetime
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- 239000004215 Carbon black (E152) Substances 0.000 title claims abstract description 40
- 229930195733 hydrocarbon Natural products 0.000 title claims abstract description 40
- 150000002430 hydrocarbons Chemical class 0.000 title claims abstract description 40
- 238000011084 recovery Methods 0.000 title claims abstract description 25
- 238000001035 drying Methods 0.000 claims abstract description 24
- 238000004140 cleaning Methods 0.000 claims abstract description 19
- 238000009833 condensation Methods 0.000 claims abstract description 17
- 230000005494 condensation Effects 0.000 claims abstract description 17
- 239000007788 liquid Substances 0.000 claims abstract description 14
- 238000003860 storage Methods 0.000 claims abstract description 13
- 238000001816 cooling Methods 0.000 claims description 15
- 239000003795 chemical substances by application Substances 0.000 claims description 10
- 239000000498 cooling water Substances 0.000 claims description 7
- 238000001914 filtration Methods 0.000 claims description 4
- 239000012530 fluid Substances 0.000 claims description 4
- 238000010079 rubber tapping Methods 0.000 claims description 3
- 238000007789 sealing Methods 0.000 claims description 2
- 238000007605 air drying Methods 0.000 description 8
- 239000000463 material Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 4
- 239000008246 gaseous mixture Substances 0.000 description 4
- 238000001704 evaporation Methods 0.000 description 3
- 235000011194 food seasoning agent Nutrition 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- AJDIZQLSFPQPEY-UHFFFAOYSA-N 1,1,2-Trichlorotrifluoroethane Chemical compound FC(F)(Cl)C(F)(Cl)Cl AJDIZQLSFPQPEY-UHFFFAOYSA-N 0.000 description 1
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000012459 cleaning agent Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000004973 liquid crystal related substance Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Images
Abstract
The utility model discloses a hydrocarbon solution recovery system. The hydrocarbon solution recovery system comprises a cleaning assembly and a recovery assembly, wherein the cleaning assembly comprises a sealed cleaning groove, a drying groove and a liquid storage groove, the liquid storage groove is communicated with the cleaning groove by a liquid supply tube, a circulation pump is arranged on the liquid supply tube, an exhaust tube is arranged on the drying groove, and an exhaust fan is arranged at the tail end of the exhaust tube; the recovery assembly comprises a vacuum pump and a condensation tank which are sequentially arranged on the exhaust tube between the drying groove and the exhaust fan, wherein the drying groove is connected to the suction end of the vacuum pump by the exhaust tube, a condensate groove, a condensation grid and an exhaust groove are sequentially formed in the condensation tank from bottom to top, the exhaust end of the vacuum pump is connected into the condensate groove in the condensation tank by the exhaust tube, a cold coiled pipe is arranged in the condensate groove, the exhaust groove is connected to the exhaust fan by the exhaust tube, and the bottom of the condensate groove is connected to the liquid storage groove by a liquid transfer tube.
Description
Technical field
The utility model relates to industry cleaning link field, refers to especially the hydrocarbon solution recovery system in a kind of cleaning equipment.
Background technology
In industrial processes, often need to clean the material strip before processing, along with the requirement to environment personal safety, outstanding cleaning agent CFC-113(fluorine Lyons of the cleaning industry being once widely used) and 1.1.1-trichloroethanes (ethane) completely forbidden production, import, use, the solvent of the hydrocarbon system such as hydrocarbon solution becomes substitute.Hydrocarbon solution is applied to the industries such as five metals, jewellery, clock and watch, automobile and motorcycle, space flight and aviation, electronics, electric, liquid crystal, semiconductor, can effectively remove various greasy dirts, grease and help weldering resin, buffing wax etc.
Traditional industry cleaning link common practices is that hydrocarbon solution is contained in the rinse bath of relative closure, when making workpiece, material strip by described rinse bath, cleaned, and at the back segment of rinse bath, one hot-air seasoning groove is set, while making workpiece or material strip through described hot-air seasoning groove, washed away oven dry by hot blast, prevent cleaning fluid to take out of, also the convenient processing that drops into immediately next stage is used.But, common cleaning equipment, only to there is rinse bath and hot-air seasoning groove, described heated-air drying groove has the hydrocarbon solution evaporation of part in the course of the work, in described heated-air drying groove, by the hot blast that blows out, described material strip or workpiece being carried out to high temperature washes away, hydrocarbon solution on workpiece or material strip is washed away and evaporated, make workpiece or material strip dry, therefore in described heated-air drying groove, can be full of air because of the hot blast blowing out, and in air, contain a large amount of hydrocarbon solution gas, and for heated-air drying groove can normally be worked, air exhauster all can be set, in order to the unnecessary air in described heated-air drying groove is extracted out.But owing to having mixed a large amount of hydrocarbon solution gas in the air in described heated-air drying groove, therefore can cause hydrocarbon solution waste to a certain extent, although and hydrocarbon solution nontoxic, also can cause the air pollution of workplace part.How to solve and extract the air in heated-air drying groove out and do not waste hydrocarbon solution and be technical problem underlying to be solved in the utility model.
Utility model content
The utility model provides a kind of hydrocarbon solution recovery system, its technical problem underlying to be solved is: in the groove sections such as the heated-air drying groove of traditional industrial washing device, can take away and be blended in airborne hydrocarbon solution gas in exhaust process, cause hydrocarbon solution waste.
For solving the problems of the technologies described above, the technical solution adopted in the utility model is:
A kind of hydrocarbon solution recovery system is provided, and it comprises:
Cleaning assembly, described cleaning assembly comprises rinse bath, drying tank and the reservoir of sealing, described reservoir is communicated with described rinse bath by feed pipe, on described feed pipe, be provided with for the cleaning fluid of described reservoir is pumped into the circulating pump in described rinse bath, described drying tank is provided with the blast pipe that is communicated with outside air, and the end of described blast pipe is provided with air exhauster;
Reclaim assembly, described recovery assembly comprises the vavuum pump on the described blast pipe being successively set between described drying tank and air exhauster, drainer, wherein, described drying tank is connected to the suction end of described vavuum pump by described blast pipe, in described drainer, be disposed with from bottom to up condensate tank, condensation grid and air discharge duct, the exhaust end of described vavuum pump is connected in the condensate tank in described drainer by described blast pipe, in described condensate tank, be provided with cooling coil, described air discharge duct is connected to described air exhauster by described blast pipe, the bottom of described condensate tank is connected to described reservoir by woven hose.
Optimal way: be positioned at position more than high liquid level (HLL) in described rinse bath and be connected with the suction end of described vavuum pump by described blast pipe.
Optimal way: be provided with the air cleaner for the airborne hydrocarbon solution gas of filtration resistance on the blast pipe between described air discharge duct and described air exhauster.
Optimal way: be perfused with agent for storage of coldness in described cooling coil, described cooling coil is connected with cooling-water machine, the input port of described cooling coil and delivery outlet are connected with agent for storage of coldness delivery outlet and the agent for storage of coldness recovery mouthful of described cooling-water machine respectively.
Optimal way: be provided with one on the described woven hose between described condensate tank and described reservoir for clearing up, discharge the tapping valve of described condensate tank liquid.
Optimal way: described drying tank is provided with the air supply pipe for high temperature, pressure-air are provided, is provided with air filter in described air supply pipe, and described air filter is provided with operated pneumatic valve between described drying tank.
Compared with prior art, the beneficial effects of the utility model are:
One, can reclaim efficiently hydrocarbon solution gas, prevent it because evaporation is rear and air mixes discharge, cause the wasting of resources;
Two, simple in structure, easy to use, use cost is low, is convenient to come into operation on a large scale;
Three, can, in recovery directly recycling afterwards, effectively form the circulation that is recycled to recycling, without intermediate treatment link.
Accompanying drawing explanation
Fig. 1 is integral frame schematic diagram of the present utility model.
The specific embodiment
Below with reference to accompanying drawing 1 and preferred embodiment, the hydrocarbon solution recovery system of the one the utility model proposes is done more to describe in detail.
As shown in Figure 1, the utility model provides a kind of hydrocarbon solution recovery system, it comprises cleaning assembly and reclaims assembly, described cleaning assembly comprises rinse bath 1, drying tank 2 and the reservoir 3 of relative closure, described reservoir 3 is communicated with described rinse bath 1 by feed pipe 4, on described feed pipe 4, be provided with for the cleaning fluid of described reservoir 3 (hydrocarbon solution) is pumped into the circulating pump 5 in described rinse bath 1, described drying tank 2 is provided with the blast pipe 6 that is communicated with outside air, and the end of described blast pipe 6 is provided with air exhauster 7, described recovery assembly comprises the vavuum pump 8 on the described blast pipe 6 being successively set between described drying tank 2 and air exhauster 7, drainer 9, wherein, described drying tank 2 is connected to the suction end of described vavuum pump 8 by described blast pipe 6, in described drainer 9, be disposed with from bottom to up condensate tank 91, condensation grid 92 and air discharge duct 93, the exhaust end of described vavuum pump 8 is connected in the condensate tank 91 in described drainer 9 by described blast pipe 6, in described condensate tank 91, be provided with cooling coil 94, described air discharge duct 93 is connected to described air exhauster 7 by described blast pipe 6, the bottom of described condensate tank 91 is connected to described reservoir 3 by woven hose 95.
The utility model in the specific implementation, described vavuum pump 8 is drawn to the HTHP gaseous mixture in drying tank 2 in described condensate tank 91, liquid congeals into the hydrocarbon solution gas cold in gaseous mixture under the cryogenic condensation effect of described cooling coil 94, and gaseous mixture in described condensate tank 91 can enter in described air discharge duct 93 through described condensation grid 92 under the double action of described air exhauster 7 and described vavuum pump 8, can will the further condensation of uncooled hydrocarbon solution gas in described condensate tank 91 under the effect of described condensation grid 92, remaining air is discharged from described air discharge duct 93, realize comprehensive the hydrocarbon solution in gaseous mixture condensation is reclaimed, and in described condensate tank 91, the hydrocarbon solution under condensation can be delivered to and in described reservoir 3, be supplied to described rinse bath 1 and reuse by described woven hose 95.
Preferred embodiment: be positioned at position more than high liquid level (HLL) in described rinse bath 1 and be connected with the suction end of described vavuum pump 8 by described blast pipe 6, and then can the hydrocarbon solution evaporating in described rinse bath 1 be carried out to condensation recovery simultaneously.
Preferred embodiment: be provided with the air cleaner 10 for the airborne hydrocarbon solution gas of filtration resistance on the blast pipe 6 between described air discharge duct 93 and described air exhauster 7, to, than the bulky hydrocarbon solution gas molecule filtration resistance of air molecule in described air discharge duct 93, prevent from discharging together with air because of a large amount of hydrocarbon solution gas that condensation rate causes not by described air cleaner 10.
Preferred embodiment: be perfused with agent for storage of coldness in described cooling coil 94, described cooling coil 94 is connected with cooling-water machine 11, the input port of described cooling coil 94 and delivery outlet are connected with agent for storage of coldness delivery outlet and the agent for storage of coldness recovery mouthful of described cooling-water machine 11 respectively, utilizing described cooling-water machine is that described cooling coil 94 upgrades agent for storage of coldness, makes described cooling coil 94 can not cause because having absorbed a large amount of heat condensation effect to decline.
Preferred embodiment: be provided with one on the described woven hose 95 between described condensate tank 91 and described reservoir 3 for clearing up, discharge the tapping valve 96 of described condensate tank 91 liquid, and then the liquid in described condensate tank 91 can be discharged and described drainer 9 is cleaned.
Preferred embodiment: described drying tank 2 is provided with the air supply pipe 21 for high temperature, pressure-air are provided, in described air supply pipe 21, be provided with air filter 22, described air filter 22 is provided with operated pneumatic valve 23 between described drying tank 2, the present embodiment can ensure that the gas entering in described drying tank 2 is clean, prevents that other impurity from remaining in described condensate tank 91 in condensation process.
Comprehensive the above, the technical solution of the utility model can fully effectively complete above-mentioned utility model object, and structural principle of the present utility model and the principle of work and power are all verified in an embodiment fully, and can reach effect and the object of expection, and embodiment of the present utility model also can convert according to these principles, therefore, the utility model comprises that all mention all replacement contents in scope in claim.Any equivalence of doing in the utility model claim changes, within all belonging to the scope of the claims of this case application.
Claims (6)
1. a hydrocarbon solution recovery system, is characterized in that comprising:
Cleaning assembly, described cleaning assembly comprises rinse bath, drying tank and the reservoir of sealing, described reservoir is communicated with described rinse bath by feed pipe, on described feed pipe, be provided with for the cleaning fluid of described reservoir is pumped into the circulating pump in described rinse bath, described drying tank is provided with the blast pipe that is communicated with outside air, and the end of described blast pipe is provided with air exhauster;
Reclaim assembly, described recovery assembly comprises the vavuum pump on the described blast pipe being successively set between described drying tank and air exhauster, drainer, wherein, described drying tank is connected to the suction end of described vavuum pump by described blast pipe, in described drainer, be disposed with from bottom to up condensate tank, condensation grid and air discharge duct, the exhaust end of described vavuum pump is connected in the condensate tank in described drainer by described blast pipe, in described condensate tank, be provided with cooling coil, described air discharge duct is connected to described air exhauster by described blast pipe, the bottom of described condensate tank is connected to described reservoir by woven hose.
2. the hydrocarbon solution recovery system of one as claimed in claim 1, is characterized in that: in described rinse bath, be positioned at position more than high liquid level (HLL) and be connected with the suction end of described vavuum pump by described blast pipe.
3. the hydrocarbon solution recovery system of one as claimed in claim 2, is characterized in that: on the blast pipe between described air discharge duct and described air exhauster, be provided with the air cleaner for the airborne hydrocarbon solution gas of filtration resistance.
4. the hydrocarbon solution recovery system of one as claimed in claim 3, it is characterized in that: in described cooling coil, be perfused with agent for storage of coldness, described cooling coil is connected with cooling-water machine, and the input port of described cooling coil and delivery outlet are connected with agent for storage of coldness delivery outlet and the agent for storage of coldness recovery mouthful of described cooling-water machine respectively.
5. the hydrocarbon solution recovery system of one as claimed in claim 4, is characterized in that: on the described woven hose between described condensate tank and described reservoir, be provided with one for clearing up, discharge the tapping valve of described condensate tank liquid.
6. the hydrocarbon solution recovery system of one as claimed in claim 5, it is characterized in that: described drying tank is provided with the air supply pipe for high temperature, pressure-air are provided, in described air supply pipe, be provided with air filter, described air filter is provided with operated pneumatic valve between described drying tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320810692.7U CN203598663U (en) | 2013-12-11 | 2013-12-11 | Hydrocarbon solution recovery system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320810692.7U CN203598663U (en) | 2013-12-11 | 2013-12-11 | Hydrocarbon solution recovery system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203598663U true CN203598663U (en) | 2014-05-21 |
Family
ID=50711364
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320810692.7U Expired - Lifetime CN203598663U (en) | 2013-12-11 | 2013-12-11 | Hydrocarbon solution recovery system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203598663U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106733871A (en) * | 2016-11-22 | 2017-05-31 | 广东新球清洗科技股份有限公司 | A kind of energy saving recovery method of agent for carbon hydrogen detergent and a kind of hydrocarbon cleaning equipment |
| 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 |
| CN109513230A (en) * | 2018-11-16 | 2019-03-26 | 江苏晓宝复合材料有限公司 | A kind of organic solvent recovery device |
-
2013
- 2013-12-11 CN CN201320810692.7U patent/CN203598663U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106733871A (en) * | 2016-11-22 | 2017-05-31 | 广东新球清洗科技股份有限公司 | A kind of energy saving recovery method of agent for carbon hydrogen detergent and a kind of hydrocarbon cleaning equipment |
| 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 |
| CN109513230A (en) * | 2018-11-16 | 2019-03-26 | 江苏晓宝复合材料有限公司 | A kind of organic solvent recovery device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C53 | Correction of patent of invention or patent application | ||
| CB03 | Change of inventor or designer information |
Inventor after: Li Liliang Inventor after: New species Inventor after: Zhang Xinxin Inventor after: Shen Zuming Inventor after: Lu Jiaao Inventor after: Min Yuanyuan Inventor before: Li Lixin Inventor before: New species Inventor before: Zhang Xinxin Inventor before: Shen Zuming Inventor before: Lu Jiaao Inventor before: Min Yuanyuan |
|
| COR | Change of bibliographic data |
Free format text: CORRECT: INVENTOR; FROM: LI LIXIN ZHONG XINQUAN ZHANG XINXIN SHEN ZUMING LU JIAAO MIN YUANYUAN TO: LI LILIANG ZHONG XINQUAN ZHANG XINXIN SHEN ZUMING LU JIAAO MIN YUANYUAN |
|
| C56 | Change in the name or address of the patentee |
Owner name: SHENZHEN GCL TECHNOLOGY CO., LTD. Free format text: FORMER NAME: SHENZHEN XINCHENGNUO TECHNOLOGY CO., LTD. |
|
| CP01 | Change in the name or title of a patent holder |
Address after: 518000 B7 building, A-5 block, Tong Sheng Industrial Park, Baoan District, Shenzhen, Guangdong, China Patentee after: SHENZHEN GCL TECH CO.,LTD. Address before: 518000 B7 building, A-5 block, Tong Sheng Industrial Park, Baoan District, Shenzhen, Guangdong, China Patentee before: SHENZHEN GCL TECHNOLOGY Co.,Ltd. |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140521 |