CN202785845U - Processing device of cooling water in oil processing extraction workshop - Google Patents
Processing device of cooling water in oil processing extraction workshop Download PDFInfo
- Publication number
- CN202785845U CN202785845U CN 201220485475 CN201220485475U CN202785845U CN 202785845 U CN202785845 U CN 202785845U CN 201220485475 CN201220485475 CN 201220485475 CN 201220485475 U CN201220485475 U CN 201220485475U CN 202785845 U CN202785845 U CN 202785845U
- Authority
- CN
- China
- Prior art keywords
- water
- cooling water
- communicated
- boiler
- extraction workshop
- 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
Links
Images
Landscapes
- Water Treatment By Sorption (AREA)
Abstract
The utility model discloses a processing device of cooling water in an oil processing extraction workshop. The processing device of the cooling water in the oil processing extraction workshop comprises filters, a head water tank and a mollifier, wherein one end of each filter is communicated with a cooling water circulation system, and the other end of each filter is communicated with one end of the head water tank; the other end of the head water tank is communicated with one end of the molllifier, and the other end of the mollifier is communicated with a boiler. According to the processing device of the cooling water in the oil processing extraction workshop, circulating cooling water with a higher temperature flowing out of the extraction workshop is recovered and is used as water to be filled in the boiler. The circulating cooling water flows through each filter, so manganese sand, activated carbon and strongly acidic materials in the water are fully filtered. After mollification of the mollifier, the circulating cooling water can be used as the water to be filled in the boiler. The operation is simple and fast, time and labor are saved, the utilization rate of heat energy is improved, the water resource is saved, the burning capacity of raw coal is reduced and the production cost is greatly saved.
Description
Technical field
The utility model belongs to the grease manufacture field, is specifically related to the treatment unit that the workshop water coolant is leached in a kind of grease processing.
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 temperature raise more to some extent after recirculated cooling water flowed out and leaches the workshop, and the temperature of the lower water coolant of long-time circulation can reach 36 ℃, its cooling efficiency to solvent also decreases, for guaranteeing the cooling efficiency of solvent, need this part water discharge point, fill into again new cold water, because this part water is leaching circulation time between workshop and refrigerating unit, constantly be heated, continuous cooling concentration, the salt concn in its water increases, if directly emit, then cause the waste of water resources, so grease processing enterprise usually reclaims this part water and as boiler replenishing water, so both saved water resources, save again heat energy, greatly reduced production cost.But contain the impurity such as manganese sand, gac and a small amount of grease in this part water, and the water quality of this part water is harder, can not be directly used in boiler replenishing water.
The utility model content
The utility model provides a kind of grease processing to leach the treatment unit of workshop water coolant for solving the deficiency of background technology, and it can get rid of the impurity in the recirculated cooling water, and can do softening the processing to recirculated cooling water, so that the boiler of feeding moisturizing is used.
The treatment unit of workshop water coolant is leached in grease processing of the present utility model, the technical scheme that adopts for the technical solution problem is: it comprises strainer, elevated tank and softening agent, strainer one end is communicated with cooling water recirculation system, the other end is communicated with an end of elevated tank, the other end of elevated tank is communicated with an end of softening agent, and the other end of softening agent is communicated with boiler.
Preferably, described strainer is made of filtration with manganese sand device, activated charcoal filter and the acidic resins strainer that head and the tail are communicated with successively.
Preferably, the quantity of described softening agent 5 is 2.
The treatment unit of workshop water coolant is leached in grease processing of the present utility model, reclaim and be used as boiler replenishing water with leaching the higher recirculated cooling water of temperature that flows out in the workshop, the temperature of the recirculated cooling water that flows out from the leaching workshop is about 36 ℃, deep well is directly supplied with the temperature of water of boiler about 16 ℃, therefore finding out with leaching the higher recirculated cooling water of temperature of discharging in the workshop comes the boiler of feeding moisturizing to use, both improved the utilization ratio of heat energy, saved again water resources, also reduced the Coal-fired capacity of heating boiler, as calculated, replenished 302.424 tons in the boiler in per 24 hours and leach the recirculated cooling waters that flow out in workshops, but every year 90728 tons of conserve water; Be that 4200 joules/Gong Jin ﹒ degree calculates by water specific heat, the temperature of the water that the boiler of feeding moisturizing is used is raised to 36 ℃ from 16 ℃, is 0.73 to calculate by boiler efficiency, and 90728 tons of water can be saved 356 tons in raw coal every year, have greatly saved production cost.Recirculated cooling water of the present utility model each strainer of flowing through, manganese sand, gac and strongly-acid material in the water are filtered out fully, again through the softening boiler of feeding moisturizing usefulness that gets final product of softening agent, the continuous cooling concentration because this part water constantly is heated between condenser and refrigerating unit, salt concn wherein increases, and salt can make water soften, so just saved in addition and in water, added the operation that salt comes softening water, saved the usage quantity of salt, further saved production cost, it is simple and efficient to handle, time saving and energy saving.
Description of drawings:
Fig. 1 is structural representation of the present utility model.
Embodiment:
With reference to Fig. 1, the treatment unit of workshop water coolant is leached in this grease processing, it is characterized in that: comprise strainer, elevated tank 4 and softening agent 5, strainer one end is communicated with cooling water recirculation system, the other end is communicated with an end of elevated tank 4, the other end of elevated tank 4 is communicated with an end of softening agent 5, and the other end of softening agent 5 is communicated with boiler.Strainer is made of filtration with manganese sand device 1, activated charcoal filter 2 and the acidic resins strainer 3 that head and the tail are communicated with successively.The quantity of softening agent 5 is 2.Pass through successively filtration with manganese sand device 1, activated charcoal filter 2 and acidic resins strainer 3 from leaching the recirculated cooling water that flows out in the workshop, three strainers filter out respectively manganese sand, gac and a small amount of grease, the strongly-acid material in the recirculated cooling water, recirculated cooling water after three strainers filter flows in the softening agent 5 through elevated tank 4, deliver in the boiler after softening agent 5 softens processing, the boiler of feeding moisturizing is used.
Claims (3)
1. a grease is processed the treatment unit that leaches the workshop water coolant, it is characterized in that: comprise strainer, elevated tank (4) and softening agent (5), strainer one end is communicated with cooling water recirculation system, the other end is communicated with an end of elevated tank (4), the other end of elevated tank (4) is communicated with an end of softening agent (5), and the other end of softening agent (5) is communicated with boiler.
2. the treatment unit of workshop water coolant is leached in a kind of grease processing as claimed in claim 1, and it is characterized in that: the filtration with manganese sand device (1) that strainer is communicated with successively by head and the tail, activated charcoal filter (2) and acidic resins strainer (3) consist of.
3. the treatment unit of workshop water coolant is leached in a kind of grease processing as claimed in claim 1, and it is characterized in that: the quantity of softening agent (5) is 2.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220485475 CN202785845U (en) | 2012-09-22 | 2012-09-22 | Processing device of cooling water in oil processing extraction workshop |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220485475 CN202785845U (en) | 2012-09-22 | 2012-09-22 | Processing device of cooling water in oil processing extraction workshop |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202785845U true CN202785845U (en) | 2013-03-13 |
Family
ID=47813151
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220485475 Expired - Fee Related CN202785845U (en) | 2012-09-22 | 2012-09-22 | Processing device of cooling water in oil processing extraction workshop |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202785845U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103988902A (en) * | 2014-05-29 | 2014-08-20 | 吴忠市物华乳品饮料有限公司 | Milk beverage production process for recycling cooling water |
| CN105502691A (en) * | 2016-01-20 | 2016-04-20 | 杨万水 | Descaling anti-corrosion water purifier in closed circulating system |
| CN105713720A (en) * | 2016-01-29 | 2016-06-29 | 吉首大学 | Cooling water circulation system for grease leaching |
| CN108203193A (en) * | 2016-12-19 | 2018-06-26 | 天津膜天膜科技股份有限公司 | A kind of cooling cycle wastewater recycling process |
-
2012
- 2012-09-22 CN CN 201220485475 patent/CN202785845U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103988902A (en) * | 2014-05-29 | 2014-08-20 | 吴忠市物华乳品饮料有限公司 | Milk beverage production process for recycling cooling water |
| CN103988902B (en) * | 2014-05-29 | 2015-11-18 | 吴忠市物华乳品饮料有限公司 | The milk beverage production technology of cooling water cycling and reutilization |
| CN105502691A (en) * | 2016-01-20 | 2016-04-20 | 杨万水 | Descaling anti-corrosion water purifier in closed circulating system |
| CN105502691B (en) * | 2016-01-20 | 2018-03-06 | 杨万水 | Scale removal anticorrosion clear water device in closed cycle system |
| CN105713720A (en) * | 2016-01-29 | 2016-06-29 | 吉首大学 | Cooling water circulation system for grease leaching |
| CN108203193A (en) * | 2016-12-19 | 2018-06-26 | 天津膜天膜科技股份有限公司 | A kind of cooling cycle wastewater recycling process |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202785845U (en) | Processing device of cooling water in oil processing extraction workshop | |
| CN204251334U (en) | A kind of waste hydrochloric acid evaporation concentration treatment system | |
| CN204211505U (en) | Sewage environment-friendly processing unit | |
| CN102001707B (en) | Method for recycling chromic acid in electroplating waste water | |
| CN104293488A (en) | Process and system for recycling kitchen waste grease | |
| CN204285803U (en) | A kind of water heater with antiscale filter | |
| CN204265996U (en) | The water circulation system of dyeing machine | |
| CN204589307U (en) | A kind of modified version regenerating alkaline etching liquid circulation and copper retrieving arrangement | |
| CN104150509B (en) | Integral type crude salt refinement unit | |
| CN202754979U (en) | Grease processing extraction workmanship cooling circulating water pool | |
| CN103830932A (en) | Tunnel type ultrasonic triple-effect reflux extraction system | |
| CN204301301U (en) | Heat pump direct-heating-type boiler | |
| CN204417451U (en) | The full-automatic regeneration treatment system of energy-saving waste lubricating oil | |
| CN208949058U (en) | A kind of coal gasification phenol wastewater ammonia still process extraction multiple treating system | |
| CN202569680U (en) | Cooling water treatment system of air compressor | |
| CN208843757U (en) | Portable type sea water desalination equipment | |
| CN103113191A (en) | Method for producing pentaerythritol by removing formaldehyde through double rectification column | |
| CN102583630A (en) | Method for treating antimony-containing waste water by modified bentonite | |
| CN202890381U (en) | Tea water countercurrent extraction system device | |
| CN205241436U (en) | Multistage flash distillation solar seawater desalination device of multiple -effect distillation | |
| CN202064016U (en) | Heat exchanger of copper electrodeposition tank | |
| CN206666314U (en) | A kind of Ecology water-making machine | |
| CN202181355U (en) | Oxyhydrogen generating device | |
| CN211492488U (en) | Plastic granules process water cooling circulation equipment | |
| CN108862800A (en) | A kind of coal gasification phenol wastewater ammonia still process extraction multiple treating system and its processing method |
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: 20130313 Termination date: 20130922 |