CN202754979U - Grease processing extraction workmanship cooling circulating water pool - Google Patents
Grease processing extraction workmanship cooling circulating water pool Download PDFInfo
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- CN202754979U CN202754979U CN 201220485481 CN201220485481U CN202754979U CN 202754979 U CN202754979 U CN 202754979U CN 201220485481 CN201220485481 CN 201220485481 CN 201220485481 U CN201220485481 U CN 201220485481U CN 202754979 U CN202754979 U CN 202754979U
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Abstract
The utility model discloses a grease processing extraction workmanship cooling circulating water pool which comprises a first water pool, a second water pool and a third water pool. The first water pool, the second water pool and the third water pool are sequentially communicated. A water cooling tower and a drug-feeding device are arranged in the first water pool. A first overflowing tube is arranged on the two-thirds height position of a partition wall of the first water poll and the second water pool. A second overflowing tube is arranged on the one-third height position of a partition wall of the second water pool and the third water pool. After subsided in the first water pool, impurities can be discharged through a discharging pipe and a sludge pump. Water sequentially flows into the second water pool through the first overflowing tube, and then flows into the third water pool through the second overflowing tube. The water flowing through the third water pool is delivered to a condenser and cools solvent in the condenser so that the solvent is liquefied. In the process, the water repeatedly flowing through the condenser and in each water pool can be again delivered to the condenser. The water is relatively high in temperature and salinity. The water is supplied to water supplement of a boiler after heated by the condenser. Therefore, water resources are saved. Besides, environment is prevented from being polluted, utilizing efficiency of heat energy is improved, and quantity of burning coals is reduced.
Description
Technical field:
The utility model belongs to the grease manufacture field, is specifically related to a kind of grease processing extract technology refrigeration cycle pond.
Background technology:
In the extract technology of grease processing, at first need to be its heating by boiler, the solvent of utilization leaching oil is different from the boiling point of mixing oil to volatilize the solvent vaporization, and then solvent is separated with mixing oil, solvent after the volatilization also needs through condensation liquefaction, so that recycle, its condensation need be adopted condenser and hydrologic cycle cooling system, and its concrete condensing mode is; The solvent cooling of cooling-water flowing in condenser is it makes solvent liquefaction, and the temperature of cooling water that flows through like this condenser raises, and returns collection place and after cooling, the condenser of again flowing through so repeatedly, constantly is liquefied solvent for the cooling of the solvent in it.The continuous cooling concentration but cooling circulating water constantly is heated, salt concn content in it increases, and because the temperature of water coolant raise more to some extent, for guaranteeing the condensation effect of solvent, also to outwards discharge a part of water, fill into again new cold water, the part water saltiness of draining is higher, also contains a small amount of grease, if directly be discharged into extraneous meeting to environment, and also waste water resource also needs this part water is recycled for fear of contaminate environment and saving water resource.
Summary of the invention:
The utility model provides a kind of grease processing extract technology refrigeration cycle pond for solving the deficiencies in the prior art.
The technical scheme that grease processing extract technology refrigeration cycle of the present utility model pond technical solution problem adopts is: grease processing extract technology refrigeration cycle pond, it is characterized in that: comprise the first pond, the second pond and the 3rd pond that are communicated with successively, be provided with water cooling tower in described the first pond, 2/3rds At The Heights of the partition wall in the first pond and the second pond are provided with the first upflow tube; / 3rd At The Heights of the partition wall in the second pond and the 3rd pond are provided with the second upflow tube, and the bottom in the first pond is provided with swash plate, and the first pond is provided with blow-off pipe away from the bottom of the second pond one side, and the domatic and blow-off pipe of swash plate is corresponding.
Preferably, also be provided with chemicals dosing plant on described the first pond.
Preferably, described blow-off pipe is communicated with and takes out sludge pump.
The beneficial effects of the utility model are: this grease processing extract technology refrigeration cycle pond, reasonable in design, impurity after the sedimentation can and be taken out sludge pump and discharge by blow-off pipe, water flows into the second pond by the first upflow tube successively, flow into the 3rd pond by the second upflow tube again, the water of clarification in the 3rd pond of flowing through can continue by the water pipe condenser of flowing through, be the cooling of the solvent in it, make solvent liquefaction, the temperature of repeatedly flowing through in this process in condenser and each pond is higher, the water that saltiness is higher need not to emit, and can again deliver to condenser, and the boiler of feeding moisturizing is used after its heating, so both saved water resources, avoid again environment, also can improve the utilization ratio of heat energy, improved the efficient of boiler, reduce the Coal-fired capacity of boiler, greatly save cost.
Description of drawings:
Fig. 1 is structural representation of the present utility model.
Embodiment:
With reference to Fig. 1, this grease processing extract technology refrigeration cycle pond, it is characterized in that: comprise the first pond 1, the second pond 2 and the 3rd pond 3 that are communicated with successively, 2/3rds At The Heights that are provided with the partition wall in water cooling tower 4, the first ponds 1 and the second pond 2 in described the first pond 1 are provided with the first upflow tube 6; The bottom that 1/3rd At The Heights of the partition wall in the second pond 2 and the 3rd pond 3 are provided with the second upflow tube 7, the first ponds 1 is provided with swash plate 8, the first ponds 1 and is provided with blow-off pipe 9 away from the bottom of the second pond 2 one sides, and the domatic and blow-off pipe 9 of swash plate 8 is corresponding.Also be provided with chemicals dosing plant 5 on the first pond 1.Blow-off pipe 9 is communicated with takes out sludge pump 10.
During implementation, flow back to the impurity sedimentation that is mixed with in the water the first pond 1 in to swash plate 8 through leaching the workshop, and through blow-off pipe 9 discharges, take out the discharge that sludge pump 10 can be convenient to sedimentation impurity.Water in the first pond 1 flows to the second pond 2 through the first upflow tube 6, flow to the 3rd pond 3 through the second upflow tube 7 again, the water that enters like this in the 3rd pond 3 is what clarify, can be by the transport pipe condenser of flowing through, through the solvent of cooling heat is passed to water in the condenser, heated current return the water cooling tower in the first pond 1, and cool off through water cooling tower, finally flow to the 3rd pond 3 behind the complete impurity of sedimentation, and the condenser of again flowing through is the cooling of the solvent in it, so repeatedly, solvent constantly is liquefied.The water coolant continuous cooling concentration of constantly being heated in this process, the salt concn in the water increases, and the temperature of water raises more to some extent, this part water is delivered in the condenser heated again, and then the boiler of feeding moisturizing is used.
Claims (3)
1. a grease is processed extract technology refrigeration cycle pond, it is characterized in that: comprise the first pond (1), the second pond (2) and the 3rd pond (3) that are communicated with successively, be provided with water cooling tower (4) in described the first pond (1), 2/3rds At The Heights of the partition wall of the first pond (1) and the second pond (2) are provided with the first upflow tube (6); / 3rd At The Heights of the partition wall of the second pond (2) and the 3rd pond (3) are provided with the second upflow tube (7), the bottom in the first pond (1) is provided with swash plate (8), the first pond (1) is provided with blow-off pipe (9) away from the bottom of the second pond (2) one sides, and the domatic and blow-off pipe (9) of swash plate (8) is corresponding.
2. a kind of grease as claimed in claim 1 is processed extract technology refrigeration cycle pond, it is characterized in that: also be provided with chemicals dosing plant (5) on the first pond (1).
3. a kind of grease as claimed in claim 1 or 2 is processed extract technology refrigeration cycle pond, and it is characterized in that: blow-off pipe (9) is communicated with takes out sludge pump (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220485481 CN202754979U (en) | 2012-09-22 | 2012-09-22 | Grease processing extraction workmanship cooling circulating water pool |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220485481 CN202754979U (en) | 2012-09-22 | 2012-09-22 | Grease processing extraction workmanship cooling circulating water pool |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202754979U true CN202754979U (en) | 2013-02-27 |
Family
ID=47734171
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220485481 Expired - Fee Related CN202754979U (en) | 2012-09-22 | 2012-09-22 | Grease processing extraction workmanship cooling circulating water pool |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202754979U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105713720A (en) * | 2016-01-29 | 2016-06-29 | 吉首大学 | Cooling water circulation system for grease leaching |
| CN108245939A (en) * | 2018-02-09 | 2018-07-06 | 大同煤矿集团有限责任公司 | Coal slime precipitation process system and water discharge method and coal mud clearing method in draining |
-
2012
- 2012-09-22 CN CN 201220485481 patent/CN202754979U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105713720A (en) * | 2016-01-29 | 2016-06-29 | 吉首大学 | Cooling water circulation system for grease leaching |
| CN108245939A (en) * | 2018-02-09 | 2018-07-06 | 大同煤矿集团有限责任公司 | Coal slime precipitation process system and water discharge method and coal mud clearing method in draining |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130227 Termination date: 20130922 |