CN218579807U - Glass fiber waste water treatment equipment - Google Patents
Glass fiber waste water treatment equipment Download PDFInfo
- Publication number
- CN218579807U CN218579807U CN202223095479.0U CN202223095479U CN218579807U CN 218579807 U CN218579807 U CN 218579807U CN 202223095479 U CN202223095479 U CN 202223095479U CN 218579807 U CN218579807 U CN 218579807U
- Authority
- CN
- China
- Prior art keywords
- pump
- intercommunication
- heater
- distilled water
- separator
- 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.)
- Active
Links
Images
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a glass fiber waste water treatment equipment belongs to vaporization system technical field, wherein, including the air supporting system, air supporting system intercommunication has first charge pump, first charge pump intercommunication has the crude liquid jar, crude liquid jar intercommunication has the second charge pump, second charge pump intercommunication has the pre-heater, the pre-heater intercommunication has distilled water pump, distilled water pump intercommunication has distilled water jar, and its beneficial effect is, this glass fiber waste water treatment equipment, through setting up air supporting system, first charge pump, crude liquid jar, second charge pump, pre-heater, distilled water pump, distilled water jar, heater and separator, air supporting system, first charge pump, crude liquid jar, second charge pump, pre-heater, distilled water pump, distilled water jar, heater and separator etc. operation series connection do, make steam heat energy obtain effective utilization to improve the utilization ratio of heat energy, reduce the waste to the resource, the effect of guarantee processing.
Description
Technical Field
The utility model relates to an evaporation system technical field, more specifically say, it relates to a glass fiber waste water treatment equipment.
Background
Due to the wide application and popularization of the glass fiber, a large amount of glass fiber wastewater, complex chemical components and emulsion with high dispersion degree and good stability are generated along with the development process of the glass fiber, so that the treatment of the wastewater has great difficulty and the development of the industry is hindered to a certain extent.
At present, the general glass fiber wastewater treatment methods mainly comprise a physical treatment method, a physicochemical treatment method and a biochemical treatment method. Wherein, the physical treatment method can only be used as the primary treatment of the glass fiber wastewater, and the effluent can not reach the secondary discharge standard; most of the physical and chemical treatment methods have the defects of large investment, high cost, complex operation and the like; the biochemical treatment method has the defects of low efficiency, sludge expansion, floating, strict operation requirements and the like, so that the development of an efficient and energy-saving glass fiber production wastewater treatment device is necessary.
SUMMERY OF THE UTILITY MODEL
Technical problem to be solved
To the deficiency that prior art exists, the utility model aims to provide a glass fiber production wastewater treatment equipment, its utensil is high-efficient, energy-conserving and the splendid characteristics of treatment effect.
(II) technical scheme
For realizing the above-mentioned purpose, the utility model provides a glass fiber waste water treatment equipment, including the air supporting system, air supporting system intercommunication has first charge pump, first charge pump intercommunication has the crude tank, crude tank intercommunication has the second charge pump, second charge pump intercommunication has the pre-heater, the pre-heater intercommunication has distilled water pump, distilled water pump intercommunication has the distilled water pitcher, distilled water pitcher intercommunication has the heater, the heater intercommunication has the separator, the separator intercommunication has the discharge pump, the discharge pump intercommunication has the stiff ware, stiff ware intercommunication has centrifuge, centrifuge intercommunication has the mother liquor pump, the mother liquor pump is connected with the paddle desiccator.
When the glass fiber production wastewater treatment equipment of the technical scheme is used, the raw liquid tank, the second feeding pump, the preheater, the distilled water pump, the distilled water tank, the heater and the separator are arranged, the air floatation system, the first feeding pump, the raw liquid tank, the second feeding pump, the preheater, the distilled water pump, the distilled water tank, the heater, the separator and the like are operated in series, so that steam heat energy is effectively utilized, the utilization rate of heat energy is improved, the waste of resources is reduced, and the treatment effect is ensured.
Further, the heater is communicated with a compressor, and the compressor is communicated with the separator.
Furthermore, the separator is communicated with a forced circulation pump, the forced circulation pump is communicated with the heater, the separator and the preheater are communicated with each other, and the forced circulation pump is an axial flow pump.
Further, the air floatation system is used for pretreating stock solution, and the stock solution tank, the distilled water tank, the separator, the thickener, the mother solution tank and the blade dryer are all steel plate rolling devices.
Further, the preheater is a heat exchanger, the heater is a plate heater, the centrifuge is a double-push centrifuge, and the first feed pump and the second feed pump, the discharge pump and the mother liquor pump are chemical centrifugal pumps.
Further, the compressor is a centrifugal compressor.
A treatment process of glass fiber production wastewater comprises the following steps:
the method comprises the following steps: the glass fiber production wastewater is firstly removed of impurities which are not beneficial to evaporation through an air floatation system, then stock solution in a stock solution tank is conveyed into a preheater through a feed pump, the stock solution enters a heater and a separator after the temperature is increased, materials entering the separator are driven to absorb heat in the heater through the action of a forced circulation pump, then boiling evaporation treatment is carried out in the separator, steam generated during evaporation rises and flows back to continuously provide heat, and concentrated solution generated during material treatment is stopped at the bottom of the separator under the influence of gravity to continuously participate in circulation.
Step two: when the concentration of the crystal slurry produced in the separator reaches a designed value, the produced crystal slurry firstly enters a thickener and then enters a centrifuge for centrifugal separation to obtain solid, the separated mother liquor enters a mother liquor tank, one part of the mother liquor returns to the front end, and the other part of the mother liquor enters a blade dryer for treatment.
(III) advantageous effects
To sum up, the utility model discloses following beneficial effect has:
1. by arranging the air floatation system, the first feeding pump, the raw liquid tank, the second feeding pump, the preheater, the distilled water pump, the distilled water tank, the heater and the separator, the air floatation system, the first feeding pump, the raw liquid tank, the second feeding pump, the preheater, the distilled water pump, the distilled water tank, the heater, the separator and the like operate in series, so that the steam heat energy is effectively utilized, the utilization rate of the heat energy is improved, the waste of resources is reduced, and the treatment effect is ensured;
2. the compressor is arranged, so that the steam can be compressed and liquefied, the subsequent treatment is convenient, and the raw liquid tank, the distilled water tank, the separator, the thickener, the mother liquid tank and the blade dryer are all arranged as steel plate rolling devices, so that the strength of the equipment in use can be guaranteed, and the use effect can be guaranteed;
3. through selecting first charge pump and second charge pump, ejection of compact pump and mother liquor pump as the chemical industry centrifugal pump, can ensure its use intensity, through selecting forced circulation pump as the axial-flow pump, can ensure the result of use of device.
Drawings
In order to clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the embodiments or the technical solutions in the prior art will be briefly described below, it is obvious that the drawings in the following description are only one embodiment of the present invention, and other drawings can be obtained by those skilled in the art without creative efforts.
Fig. 1 is a schematic structural view of the process unit of the present invention.
The labels in the figures are:
1. an air flotation system; 2. a first feed pump; 3. a stock solution tank; 4. a second feed pump; 5. a preheater; 6. a distilled water pump; 7. a distilled water tank; 8. a heater; 9. a separator; 10. a forced circulation pump; 11. a compressor; 12. a discharge pump; 13. a thickener; 14. a centrifuge; 15. a mother liquor tank; 16. a mother liquor pump; 17. a paddle dryer.
Detailed Description
To make the utility model easy to understand and understand the technical means, creation characteristics, achievement purpose and efficacy, and is right below the utility model is implemented
The present invention will now be described in detail with reference to the accompanying drawings, wherein like reference numerals designate like parts throughout the several views.
Example (b):
the present invention will be described in further detail with reference to fig. 1.
Referring to fig. 1, the present invention provides a technical solution: the utility model provides a glass fiber production waste water treatment equipment, including air supporting system 1, air supporting system 1 intercommunication has first charge pump 2, first charge pump 2 intercommunication has former feed tank 3, former feed tank 3 intercommunication has second charge pump 4, second charge pump 4 intercommunication has pre-heater 5, pre-heater 5 intercommunication has distilled water pump 6, distilled water pump 6 intercommunication has distilled water jar 7, distilled water jar 7 intercommunication has heater 8, heater 8 intercommunication has separator 9, separator 9 intercommunication has discharge pump 12, discharge pump 12 intercommunication has thickener 13, thickener 13 intercommunication has centrifuge 14, centrifuge 14 intercommunication has mother liquor pump 16, mother liquor pump 16 is connected with paddle dryer 17, through setting up air supporting system 1, first charge pump 2, former feed pump 3, second charge pump 4, pre-heater 5, distilled water pump 6, distilled water jar 7, heater 8 and separator 9, air supporting system 1, first charge pump 2, former feed pump 3, second charge pump 4, pre-heater 5, distilled water pump 6, heater 7, distilled water pump 8 and separator 9 etc. operation series connection work, make the steam energy utilization of water jar 4, thereby the effective utilization of heat energy is ensured, thereby the utilization of the steam can be improved, thereby the utilization efficiency of the heat energy utilization is improved, the waste of the treatment of water jar, thereby the waste is ensured.
Specifically, the heater 8 is communicated with a compressor 11, the compressor 11 is communicated with a separator 9, the separator 9 is communicated with a forced circulation pump 10, the forced circulation pump 10 is communicated with the heater 8, the separator 9 and the preheater 5 are communicated with each other, and the forced circulation pump 10 is an axial flow pump.
Through adopting above-mentioned technical scheme, through setting up compressor 11, can compress the liquefaction to steam, conveniently carry out subsequent processing.
Specifically, the air flotation system 1 is a stock solution pretreatment, the stock solution tank 3, the distilled water tank 7, the separator 9, the thickener 13, the mother liquor tank 15 and the paddle dryer 17 are all steel plate rolling devices, the preheater 5 is a heat exchanger, the heater 8 is a plate heater, the centrifuge 14 is a double-push centrifuge, and the first feed pump 2, the second feed pump 4, the discharge pump 12 and the mother liquor pump 16 are all chemical centrifugal pumps.
Through adopting above-mentioned technical scheme, through all setting up raw liquor tank 3, distilled water jar 7, separator 9, stiff ware 13, mother liquor jar 15 and paddle desiccator 17 into the device that the steel sheet was rolled up, can ensure the intensity of equipment when using, can ensure the result of use.
Specifically, the compressor 11 is a centrifugal compressor.
Through adopting above-mentioned technical scheme, through selecting first charge pump 2 and second charge pump 4, discharge pump 12 and mother liquor pump 16 as the chemical industry centrifugal pump, can ensure its use intensity, through selecting forced circulation pump 10 as the axial-flow pump, can ensure the result of use of device.
A treatment process of glass fiber production wastewater comprises the following steps:
the method comprises the following steps: the glass fiber production wastewater is firstly removed of impurities which are not beneficial to evaporation through the air flotation system 1, then raw liquor in the raw liquor tank 3 is conveyed into the preheater 5 through the feed pump, the raw liquor enters the heater 8 and the separator 9 after the temperature is raised, the raw liquor entering the separator 9 drives the raw liquor to absorb heat in the heater 8 under the action of the forced circulation pump 10, then the raw liquor is boiled and evaporated in the separator 9, steam generated during evaporation rises and flows back to continuously provide heat, and concentrated liquor generated during material treatment stays at the bottom of the separator 9 under the influence of gravity to continuously participate in circulation.
Step two: when the concentration of the crystal slurry generated in the separator 9 reaches the designed value, the generated crystal slurry firstly enters the thickener 13 and then enters the centrifuge 14 for centrifugal separation to obtain solid, the separated mother liquor enters the mother liquor tank 15, one part of the mother liquor returns to the front end, and the other part of the mother liquor enters the paddle dryer 17 for treatment.
The utility model discloses a theory of operation does:
the glass fiber production wastewater is firstly removed impurities which are not beneficial to evaporation through an air floatation system 1, then raw liquid in a raw liquid tank 3 is conveyed into a preheater 5 through a feed pump, the raw liquid enters a heater 8 and a separator 9 after the temperature is increased, materials entering the separator 9 are driven to absorb heat in the heater 8 through the action of a forced circulation pump 10, then boiling evaporation treatment is carried out in the separator 9, steam generated during evaporation rises and flows back to continuously provide heat, concentrated liquid generated by material treatment stays at the bottom of the separator 9 under the influence of gravity to continuously participate in circulation, when the concentration of crystal slurry generated by treatment in the separator 9 reaches a design value, the generated crystal slurry firstly enters a thickener 13 and then enters a centrifuge 14, centrifugal separation is carried out to obtain solid, the separated mother liquid enters a mother liquid tank 15, one part of the mother liquid returns to the front end, and the other part of the mother liquid enters a paddle dryer 17 for treatment.
The specific embodiments are only for explaining the present invention, and it is not a limitation to the present invention, and those skilled in the art can make modifications to the embodiments without inventive contribution as required after reading the present specification, but all the embodiments are protected by patent law within the scope of the claims of the present invention.
Claims (6)
1. The utility model provides a glass fiber waste water treatment equipment, includes air supporting system (1), its characterized in that: the air flotation system (1) intercommunication has first charge pump (2), first charge pump (2) intercommunication has former feed tank (3), former feed tank (3) intercommunication has second charge pump (4), second charge pump (4) intercommunication has pre-heater (5), pre-heater (5) intercommunication has distilled water pump (6), distilled water pump (6) intercommunication has distilled water jar (7), distilled water jar (7) intercommunication has heater (8), heater (8) intercommunication has separator (9), separator (9) intercommunication has discharge pump (12), discharge pump (12) intercommunication has thickener (13), thickener (13) intercommunication has centrifuge (14), centrifuge (14) intercommunication has mother liquor pump (16), mother liquor pump (16) are connected with paddle desicator (17).
2. The glass fiber production wastewater treatment equipment according to claim 1, characterized in that: the heater (8) is communicated with a compressor (11), and the compressor (11) is communicated with the separator (9).
3. The glass fiber production wastewater treatment device according to claim 1, wherein: the separator (9) is communicated with a forced circulation pump (10), the forced circulation pump (10) is communicated with the heater (8), the separator (9) and the preheater (5) are communicated with each other, and the forced circulation pump (10) is an axial flow pump.
4. The glass fiber production wastewater treatment equipment according to claim 1, characterized in that: the air floatation system (1) is used for pretreating stock solution, and the stock solution tank (3), the distilled water tank (7), the separator (9), the thickener (13), the mother solution tank (15) and the blade dryer (17) are all devices for rolling steel plates.
5. The glass fiber production wastewater treatment device according to claim 1, wherein: the preheater (5) is a heat exchanger, the heater (8) is a plate heater, the centrifuge (14) is a double-push centrifuge, and the first feed pump (2), the second feed pump (4), the discharge pump (12) and the mother liquor pump (16) are chemical centrifugal pumps.
6. The glass fiber production wastewater treatment device according to claim 2, wherein: the compressor (11) is a centrifugal compressor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202223095479.0U CN218579807U (en) | 2022-11-22 | 2022-11-22 | Glass fiber waste water treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202223095479.0U CN218579807U (en) | 2022-11-22 | 2022-11-22 | Glass fiber waste water treatment equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN218579807U true CN218579807U (en) | 2023-03-07 |
Family
ID=85378840
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202223095479.0U Active CN218579807U (en) | 2022-11-22 | 2022-11-22 | Glass fiber waste water treatment equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN218579807U (en) |
-
2022
- 2022-11-22 CN CN202223095479.0U patent/CN218579807U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103073163B (en) | Treatment and sludge reduction device and method of de-sizing wastewater | |
| CN107619078B (en) | Device for treating acidic wastewater by adopting concentration stripping method | |
| CN203355316U (en) | Continuous quarternary-stage evaporation and crystallization device for manufacturing sodium gluconate | |
| CN103880211B (en) | A kind of recycling treatment process containing magnesium high-salt wastewater | |
| CN218579807U (en) | Glass fiber waste water treatment equipment | |
| CN101935080B (en) | High-concentration ammonia nitrogen blowoff treatment system | |
| CN201971688U (en) | Silicon and oil removing system for oily sewage | |
| CN104176714B (en) | A kind of method adopting reverse osmosis method to concentrate titanium white waste acid | |
| CN219449369U (en) | Skid-mounted high-power concentrated solution treatment device | |
| CN102153224A (en) | Treatment technology for industrial sewage from sodium carboxymethylcellulose | |
| CN216513299U (en) | High COD effluent treatment plant of high salt | |
| CN102392381B (en) | Chemi-mechanical pulp waste liquid alkaline recycling pretreatment method | |
| CN203513310U (en) | Rectifying separating system of hydrochloric acid wastewater | |
| CN210764959U (en) | Liquid sewage sludge treatment device | |
| CN110563222A (en) | Electric flocculation air flotation machine | |
| CN202440401U (en) | Anti-scaling disposal system for concentrating high-concentrated seawater into saturated bittern | |
| CN214714417U (en) | High-efficient solid-liquid separation equipment | |
| CN204644034U (en) | A kind of for the wastewater treatment in fuel-burning power plant and the combined apparatus of sea water desaltination | |
| CN216472686U (en) | Epoxy waste water treatment equipment | |
| CN212440107U (en) | Device for rectifying and separating acidic materials | |
| CN216038723U (en) | MVR evaporation system for concentrated solution treatment | |
| CN220845838U (en) | Fluorescent wastewater concentration device | |
| CN204125192U (en) | The useless time sodium recycle device of acetylene | |
| CN217947874U (en) | DMAC waste water multiple-effect rectification device | |
| CN213231929U (en) | Low-energy-consumption environment-friendly alcohol tank liquid recycling system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |