CN204064029U - A kind of industrial waste water disposal device - Google Patents
A kind of industrial waste water disposal device Download PDFInfo
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- CN204064029U CN204064029U CN201420400283.4U CN201420400283U CN204064029U CN 204064029 U CN204064029 U CN 204064029U CN 201420400283 U CN201420400283 U CN 201420400283U CN 204064029 U CN204064029 U CN 204064029U
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- heat exchanger
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- pump
- cooling tower
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- 239000010842 industrial wastewater Substances 0.000 title claims abstract description 69
- 238000001816 cooling Methods 0.000 claims abstract description 59
- 239000007921 spray Substances 0.000 claims abstract description 31
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 60
- 238000010521 absorption reaction Methods 0.000 claims description 10
- 238000010438 heat treatment Methods 0.000 claims description 8
- 239000002351 wastewater Substances 0.000 claims description 8
- 239000000498 cooling water Substances 0.000 claims description 5
- 239000002826 coolant Substances 0.000 claims description 4
- 238000005057 refrigeration Methods 0.000 claims description 2
- 238000012423 maintenance Methods 0.000 abstract description 6
- 230000015572 biosynthetic process Effects 0.000 abstract description 4
- 238000004064 recycling Methods 0.000 abstract description 4
- 239000003507 refrigerant Substances 0.000 description 9
- 239000006096 absorbing agent Substances 0.000 description 7
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 description 6
- 239000010865 sewage Substances 0.000 description 5
- 238000001704 evaporation Methods 0.000 description 4
- 230000008020 evaporation Effects 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 229940059936 lithium bromide Drugs 0.000 description 3
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 229910052744 lithium Inorganic materials 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000004438 eyesight Effects 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model discloses a kind of industrial waste water disposal device, the tank of its cooling tower is communicated with industrial wastewater, and be communicated with spray pipeline by the first pump, so that industrial wastewater is pumped into spray pipeline, the second medium runner of First Heat Exchanger is used for being communicated with high-temperature medium to be cooled, second heat exchanger is installed on the air inlet of cooling tower, and form annular channel with the second medium flow passage of First Heat Exchanger, second pump is arranged between the media outlet of second medium runner and the medium inlet of the second heat exchanger, to drive circulatory mediator at annular channel internal circulation flow.Compared with prior art, First Heat Exchanger is communicated with formation closed cycle heat-exchange system with the second heat exchanger, realize on heat propagation function basis, industrial wastewater only circulates between the spray pipeline of cooling tower and tank, and be not directly communicated with heat exchanger, thus solve the medium runner scale problems of heat exchanger, decrease the maintenance times of heat exchanger, and then reduce the cost recycling industrial wastewater.
Description
Technical field
The utility model relates to industrial waste water treatment, particularly a kind of industrial waste water disposal device.
Background technology
Industrial wastewater refers to the waste water, sewage and the waste liquid that produce in industrial processes, wherein containing the pollutant produced in the industrial production materials, intermediate product and the product that outflow with water and production process.Along with developing rapidly of industry, kind and the quantity of waste water rapidly increase, also increasingly extensive and serious to the pollution of water body, threaten the health and safety of the mankind.Therefore, for protection of the environment, the process of industrial wastewater is more even more important than the process of municipal sewage.
Existing composition graphs 1, a kind of industrial sewage processing unit comparatively conventional before improving eyesight and processing method thereof.
As shown in Figure 1, this device comprises cooling tower 1 ', heat-exchangers of the plate type 2 ', pump 3 ' and is communicated with the pipeline of three, wherein, tower body 11 ' the bottom of cooling tower 1 ' has the tank 12 ' be communicated with industrial wastewater, its tank 12 ' is communicated with the second medium runner 21 ' of plate type heat exchanger 2 ', its spray pipeline 13 ' is by pump 3 ' and second medium runner 21 ', and the first medium runner 21 ' of plate type heat exchanger 2 ' is communicated with high-temperature medium to be cooled.
The operation principle of this device is, interior for cooling tower 1 ' industrial wastewater is pumped into the second medium runner 22 ' of plate type heat exchanger 2 ' by pump 3 ', meanwhile, high-temperature medium to be cooled flows into first medium runner 21 ', the industrial wastewater that second medium runner 22 ' is interior and the interior high-temperature medium of first medium runner 21 ' carry out heat exchange in plate type heat exchanger 2 ', high-temperature medium is back to equipment to be cooled after meeting cold formation cryogenic media continues to use, through being sprayed by spray pipeline 13 ' after industrial wastewater heat absorption heats up.Then, the hot industry waste water sprayed out with enter the interior cold air of cooling tower 1 ' and to meet generation heat exchange, the evaporation of part industrial wastewater is discharged by exhaust outlet under exhaust fan 14 ' acts on the air heated up after heat absorption, is back in the tank 12 ' of cooling tower after residue heat release cooling.
Obviously, trade effluent is recycled as heat exchange medium by this device, avoids and directly discharges and the environmental pollution that causes and energy loss.But industrial wastewater directly contacts with plate type heat exchanger 2 ' in the apparatus, very easily fouling in plate type heat exchanger 2 ' runner.In order to ensure that this device normally runs, the heat exchanger monthly need shut down cleaning 1 ~ 2 time or more renew before reaching its specified service life, obviously, certainly will cause like this and recycle the high problem of industrial wastewater cost.
In view of this, those skilled in the art urgently carry out structure optimization to existing industrial waste water disposal device, to reduce the cost reclaiming and utilize industrial wastewater.
Utility model content
For above-mentioned defect, core object of the present utility model is, provides a kind of industrial waste water disposal device, to reduce the cost reclaiming and utilize industrial wastewater.
In order to achieve the above object, industrial waste water disposal device provided by the utility model, comprise cooling tower and First Heat Exchanger, the tank of described cooling tower is communicated with described industrial wastewater, the first flow of described First Heat Exchanger is used for being communicated with high-temperature medium to be cooled, it is characterized in that, also comprise:
At least one second heat exchanger, is installed on the air inlet of described cooling tower, and forms annular channel with the second flow passage of described First Heat Exchanger;
First pump, between the spray pipeline being arranged at described tank and described cooling tower, to pump into described spray pipeline by described industrial wastewater;
Second pump, is arranged between the media outlet of described First Heat Exchanger and the medium inlet of described second heat exchanger, to drive described circulatory mediator at described annular channel internal circulation flow.
Preferably, be hung on outside the tower body of described cooling tower outside described second heat exchanger.
Preferably, the tower body four sides of described cooling tower all offers air inlet, and each described air inlet is provided with described second heat exchanger.
Preferably, described cooling tower is no-arbitrary pricing formula cooling tower.
Preferably, described cooling tower also comprises the water collection device be arranged at above described spray pipeline.
Preferably, also comprise Wastewater Pretreatment unit, described Wastewater Pretreatment unit comprises collecting-tank and overflow pipe, and described collecting-tank is communicated with by described overflow pipe with described tank, and described overflow pipe is positioned at above at the bottom of the pond of described tank.
Preferably, also comprise circulatory mediator temperature-adjusting device, be arranged between described First Heat Exchanger and the second heat exchanger, to adjust the temperature of described annular channel Inner eycle medium.
Preferably, described circulatory mediator temperature-adjusting device comprises first-class absorption type heat pump and the 3rd pump, the heat source water entrance of described first-class absorption type heat pump is communicated with the media outlet of the second medium runner of described First Heat Exchanger, the outlet of its heat source water is communicated with the medium inlet of the second medium runner of described First Heat Exchanger, its hot water inlet is communicated with the media outlet of described second heat exchanger, its hot water outlet is communicated with the medium inlet of described second pump, its steam inlet and solidifying water out are used for being communicated with outside heating plant, between the media outlet that described 3rd pump is arranged at the second medium runner of described First Heat Exchanger and described hot water inlet.
Preferably, described circulatory mediator temperature-adjusting device comprises second-kind absorption-type heat pump and the 4th pump, the heat source water entrance of described second-kind absorption-type heat pump is communicated with the media outlet of the second medium runner of described First Heat Exchanger, the outlet of its heat source water is communicated with the medium inlet of the second medium runner of described First Heat Exchanger, its hot water inlet is communicated with the media outlet of described second heat exchanger, its hot water outlet is communicated with the medium inlet of described second pump, its cooling water inlet and coolant outlet are used for being communicated with external refrigeration device, between the media outlet that described 4th pump is arranged at the second medium runner of described First Heat Exchanger and described hot water inlet.
Preferably, described medium temperature adjusting device comprises auxiliary cooling tower and the 3rd heat exchanger, described 3rd heat exchanger to be installed in described auxiliary cooling tower and to be positioned at below spray pipeline, and its medium inlet is communicated with described second heat exchanger, and its media outlet is communicated with described First Heat Exchanger.
Industrial waste water disposal device provided by the utility model, comprise industrial sewage processing unit and comprise circulatory mediator, cooling tower, First Heat Exchanger, second heat exchanger, first pump and the second pump, wherein, the tank of cooling tower is communicated with industrial wastewater, and be communicated with spray pipeline by the first pump, spray after industrial wastewater is pumped into spray pipeline, the second medium runner of First Heat Exchanger is used for being communicated with high-temperature medium to be cooled, second heat exchanger is installed on the air inlet of cooling tower, and form annular channel with the second medium flow passage of First Heat Exchanger, second pump is arranged between the media outlet of second medium runner and the medium inlet of the second heat exchanger, to drive circulatory mediator at annular channel internal circulation flow.
Compared with prior art, this programme is communicated with formation closed cycle heat-exchange system by First Heat Exchanger with the second heat exchanger, realizing on heat propagation function basis, industrial wastewater only circulates between the spray pipeline of cooling tower and tank, and flow passage that is not direct and heat exchanger, solve the medium runner scale problems of heat exchanger, the maintenance times decreasing heat exchanger extends its actual life simultaneously, thus indirectly reduces the cost reclaiming and utilize industrial wastewater.
Accompanying drawing explanation
Fig. 1 illustrates the structural representation of existing industrial waste water disposal device;
Fig. 2 shows the structural representation of industrial waste water disposal device first detailed description of the invention provided by the utility model;
Fig. 3 shows the plan structure schematic diagram of cooling tower shown in Fig. 2;
Fig. 4 shows the structural representation of industrial waste water disposal device second detailed description of the invention provided by the utility model;
Fig. 5 shows the structural representation of industrial waste water disposal device provided by the utility model 3rd detailed description of the invention;
Fig. 6 shows the structural representation of industrial waste water disposal device provided by the utility model 4th detailed description of the invention.
Corresponding relation in Fig. 1 between Reference numeral and all parts title:
1 ' cooling tower, 11 ' tower body, 12 ' tank, 13 ' spray pipeline, 14 ' exhaust fan, 2 ' plate type heat exchanger, 21 ' first medium runner, 22 ' second medium runner, 3 ' pump.
Corresponding relation in Fig. 2 to Fig. 6 between Reference numeral and all parts title:
1 cooling tower, 11 tower bodies, 12 tanks, 13 spray pipelines, 14 exhaust fans, 2 First Heat Exchangers, 21 first medium runners, 22 second medium runners, 3 second heat exchangers, 4 first pumps, 5 second pumps, 6 second-kind absorption-type heat pumps, A
inheat source water entrance, A
outheat source water outlet, B
inhot water inlet, B
outhot water outlet, H
insteam inlet, H
outsolidifying water out, 7 the 3rd pumps, 8 second-kind absorption-type heat pumps, D
inheat source water entrance, D
outheat source water outlet, E
inhot water inlet, E
outhot water outlet, C
incooling water inlet, C
outcoolant outlet, 9 the 4th pumps, G auxiliary cooling tower, I the 3rd heat exchanger.
Detailed description of the invention
Core of the present utility model is, improves a kind of industrial waste water disposal device, to reduce the recycling cost of industrial wastewater.
Described in this programme and cooling tower concrete structure and operation principle identical with prior art, so do not repeat them here, now describe concrete structure and the operation principle thereof of industrial waste water disposal device in detail in conjunction with Figure of description herein.It should be noted that, in Figure of description, arrow " " refers to the flow direction of pipeline medium, is appreciated that the appearance of this arrow does not limit protection domain of the present utility model.In addition, addressed herein circulatory mediator can be recirculated water or other meet the medium of technological requirement.
Refer to Fig. 2 and Fig. 3, wherein, Fig. 2 shows the structural representation of industrial waste water disposal device first detailed description of the invention provided by the utility model, and Fig. 3 shows the plan structure schematic diagram of cooling tower shown in Fig. 2.
As shown in Figure 2, industrial sewage processing unit comprises cooling tower 1, First Heat Exchanger 2, second heat exchanger 3, first pump 4 and the second pump 5, wherein, the tank 12 of cooling tower 1 is communicated with industrial wastewater, and be communicated with spray pipeline 13 by the first pump 4, spray after industrial wastewater being pumped into spray pipeline 13, the second medium runner 22 of First Heat Exchanger 2 is for being communicated with high-temperature medium to be cooled, second heat exchanger 3 is installed on the air inlet of cooling tower 1, and be communicated with the second medium runner 22 of First Heat Exchanger 2 and form annular channel, second pump 5 is arranged between the media outlet of second medium runner 22 and the medium inlet of the second heat exchanger 3, to drive circulatory mediator at closed ring runner internal circulation flow.For the ease of understanding the structure of this device better, please also refer to Fig. 3.
Low-temperature circulating medium heat exchanges when high-temperature medium to be cooled flows through first medium runner 21 and in second medium runner 22, and cooled high-temperature medium is back in equipment to be cooled.Low-temperature circulating medium after meanwhile heating up flows through the second heat exchanger 3, with the cold air heat exchange entered by air inlet in tower body 11, high temperature air is formed after cold air is absorbed heat, this high temperature air carries out heat exchange with the industrial wastewater sprayed by spray pipeline 13, part industrial wastewater is heated up evaporate and discharged by exhaust outlet under exhaust fan effect with high-temperature gas, remainder is back in tank 12.And cool via First Heat Exchanger 2 pairs of high temperature media to be cooled again with the low-temperature circulating water after cold air heat exchange.
Compared with prior art, this programme is communicated with formation closed cycle heat-exchange system by First Heat Exchanger 2 with the second heat exchanger 3, realizing on heat propagation function basis, industrial wastewater only circulates between the spray pipeline 13 of cooling tower 1 and tank 12, and flow passage that is not direct and heat exchanger, solve the medium runner scale problems of heat exchanger, the maintenance times decreasing heat exchanger extends its actual life simultaneously, thus greatly reduces the cost recycling industrial wastewater.
It should be noted that, cooling tower 1 in this programme is no-arbitrary pricing formula cooling tower, to avoid when industrial wastewater flows through filler impurity in it be attached to filling surface and form the generation of scale problems, the maintenance times of cooling tower 1 can be reduced like this, thus the operation and maintenance cost of this device can be create a further reduction, and then reduce the cost recycling industrial wastewater.
In addition, as shown in Figure 3, tower body 11 four sides of cooling tower 1 all offers air inlet, and is all provided with the second heat exchanger 3 at each air inlet, obviously, can improve heat transfer efficiency like this, then improve the evaporation efficiency of industrial wastewater.
Further, be hung on outside cooling tower 1 tower body 11 outside second heat exchanger 3, particularly, tower body 11 surrounding has all been connected horizontal supporting plate, by modes such as bolt assembly, welding or riveted joints, the second heat exchanger 3 is fixed on this horizontal supporting plate again, setting like this can be avoided because industrial wastewater sprays the problem of shape fouling to the second heat exchanger 3 surface, thus can ensure heat transfer efficiency and the service life of the second heat exchanger 3.
Additionally, be provided with water collection device 15 in cooling tower 1, this water collection device 15 is the top of spray pipeline 13, can prevent industrial wastewater from dispersing in environment, be of value to protection of the environment after arranging water collection device.In addition, impurity content in industrial wastewater is reduced before making to enter the first pump, this device also comprises Wastewater Pretreatment unit, specifically comprise collecting-tank 16 and overflow pipe 17, collecting-tank 16 is communicated with by overflow pipe 17 with tank 12, and overflow pipe 17 is positioned at above at the bottom of the pond of tank 12, so before industrial wastewater flows into spray pipeline 13, pretreatment can be carried out to it, i.e. part impurity sedimentation in it, thus the amount of scale buildup in spray pipeline 13 can be reduced, reduce the maintenance cost of device entirety.
Further, in order to accelerate the evaporation efficiency of industrial wastewater, this programme by setting up circulatory mediator thermostat unit in this device, the circulatory mediator temperature variation flowing through the second heat exchanger 3 is made to be not simple by medium temperature decision in First Heat Exchanger, but carry out double action with in conjunction with circulatory mediator thermostat unit, to make to meet in cooling tower the actual temperature of evaporating needed for industrial wastewater.
Existing composition graphs 4 to Fig. 6, describes multiple embodiments of circulatory mediator thermostat unit respectively in detail.Wherein, Fig. 4 shows the structural representation of industrial waste water disposal device second detailed description of the invention provided by the utility model, Fig. 5 shows the structural representation of industrial waste water disposal device provided by the utility model 3rd detailed description of the invention, and Fig. 6 shows the structural representation of industrial waste water disposal device provided by the utility model 4th detailed description of the invention.
Embodiment 1:
Circulatory mediator temperature-adjusting device comprises first-class absorption type heat pump 6 and the 3rd pump 7, the heat source water entrance A of first-class absorption type heat pump 6
inbe communicated with the media outlet of the second medium runner of First Heat Exchanger 2, its heat source water outlet A
outbe communicated with the medium inlet of the second medium runner of First Heat Exchanger 2, its hot water inlet B
inbe communicated with the media outlet of the second heat exchanger 3, its hot water outlet B
outbe communicated with the medium inlet of the second pump 5, its steam inlet H
inwith solidifying water out H
outfor being communicated with outside heating plant, the 3rd pump 7 is arranged at media outlet and the heat source water entrance A of the second medium runner of First Heat Exchanger 1
inbetween.
First-class absorption type heat pump take steam as driving heat source, in generator, heat bromize lithium dilute solution and produce refrigerant vapour, refrigerant vapour enters condenser and heats the hot water flowed through in condenser thermal transfer pipe, i.e. the second heat exchanger 3 Inner eycle medium), self be condensed into liquid deutomerite and flow to into evaporimeter.Water as refrigerant sprays evaporator heat transfer tube-surface through cryogenic fluid pump, absorbs and flows through low-temperature heat source water in heat-transfer pipe, i.e. the heat of the second medium runner 22 Inner eycle medium of First Heat Exchanger 2, flows out unit after its temperature is reduced.Water as refrigerant is vaporized into condensed steam after absorbing heat, enters absorber.Spray after being returned absorber by the lithium-bromide solution after generator concentrates, absorb the refrigerant vapour of coming from evaporimeter, and release heat, heating flows through the hot water of absorber heat-transfer pipe, the i.e. circulatory mediator of the second heat exchanger), hot water heats up flow back to the second heat exchanger through absorber, condenser.
Embodiment 2:
Circulatory mediator temperature-adjusting device comprises second-kind absorption-type heat pump 8 and the 3rd pump 9, the heat source water entrance D of second-kind absorption-type heat pump 8
inbe communicated with the media outlet of the second medium runner of First Heat Exchanger 2, its heat source water outlet D
outbe communicated with the medium inlet of the second medium runner of First Heat Exchanger 2, its hot water inlet E
inbe communicated with the media outlet of the second heat exchanger 3, its hot water outlet E
outbe communicated with the medium inlet of the second pump 5, its cooling water inlet C
inwith coolant outlet C
outfor being communicated with outside heating plant, the 3rd pump 9 is arranged at media outlet and the heat source water entrance D of the second medium runner of First Heat Exchanger 1
inbetween.
Second-kind absorption-type heat pump, is that for driving heat source, first heat source water enters evaporimeter with heat source water (i.e. the second medium runner 22 Inner eycle medium of First Heat Exchanger 2), heats cryogen and produce refrigerant vapour in evaporimeter.Refrigerant vapour enters absorber, absorbed by the bromize lithium concentrated solution from generator, and release heat, thus add the circulatory mediator (namely being flowed into the circulatory mediator of heat pump by the second heat exchanger 3) in heat absorber heat-transfer pipe, this circulatory mediator again flows back to the second heat exchanger 3 after heating up.The thinning lithium-bromide solution absorbed after cryogen enters generator through solution heat exchanger, by come flash-pot heat source water heating concentrated, and produce refrigerant vapour, refrigerant vapour enters condenser and is condensed into liquid by the cooling water in its pipe, then evaporimeter is sent into through cryogenic fluid pump, the lithium-bromide solution be concentrated is sent back to again absorber and absorbs, thus completes circulation.
It should be noted that, first-class absorption type heat pump and second-kind absorption-type heat pump are ripe existing product, and those skilled in the art can choose according to actual temperature demand in cooling tower in this device.
Embodiment 3:
Temperature-adjusting device comprises auxiliary cooling tower G and the 3rd heat exchanger I, 3rd heat exchanger I to be installed in auxiliary cooling tower G and to be positioned at below spray pipeline 13, and its medium inlet is communicated with the media outlet of the second heat exchanger 3, and its media outlet is communicated with the medium inlet of First Heat Exchanger 2.
In closed ring runner when the cooled circulatory mediator of the second heat exchanger 3 flows through the 3rd heat exchanger I, carry out after cooling makes circulatory mediator temperature drop to predetermined temperature by auxiliary cooling tower G to it, then flow in First Heat Exchanger 2 and treat cooling down high-temperature medium and implement cooling.
The foregoing is only preferred embodiment of the present utility model, do not form the restriction to the utility model protection domain.Any do within spirit of the present utility model and principle any amendment, equivalent to replace and improvement etc., all should be included within claims of the present utility model.
Claims (10)
1. industrial waste water disposal device, comprise cooling tower (1) and First Heat Exchanger (2), the tank (12) of described cooling tower (1) is communicated with described industrial wastewater, the first medium runner (21) of described First Heat Exchanger (2) is for being communicated with high-temperature medium to be cooled, it is characterized in that, also comprise:
At least one second heat exchanger (3), is installed on the air inlet of described cooling tower (1), and is communicated with the second medium runner (22) of described First Heat Exchanger (2) and forms annular channel;
First pump (4), between the spray pipeline (13) being arranged at described tank (12) and described cooling tower (1), to pump into described spray pipeline (13) by described industrial wastewater;
Second pump (5), is arranged between the media outlet of described First Heat Exchanger (2) and the medium inlet of described second heat exchanger (3), to drive circulatory mediator at described annular channel internal circulation flow.
2. industrial waste water disposal device as claimed in claim 1, is characterized in that, be hung on the tower body (11) of described cooling tower (1) outward outside described second heat exchanger (3).
3. industrial waste water disposal device as claimed in claim 2, is characterized in that, tower body (11) four sides of described cooling tower (1) all offers air inlet, and each described air inlet is provided with described second heat exchanger (3).
4. industrial waste water disposal device as claimed in claim 1, it is characterized in that, described cooling tower (1) is no-arbitrary pricing formula cooling tower.
5. industrial waste water disposal device as claimed in claim 1, is characterized in that, described cooling tower also comprises the water collection device (15) being arranged at described spray pipeline (13) top.
6. industrial waste water disposal device as claimed in claim 1, it is characterized in that, also comprise Wastewater Pretreatment unit, described Wastewater Pretreatment unit comprises collecting-tank (16) and overflow pipe (17), described collecting-tank (16) is communicated with by described overflow pipe (17) with described tank (12), and described overflow pipe (17) is positioned at above at the bottom of the pond of described tank (12).
7. the industrial waste water disposal device according to any one of claim 1 to 6, it is characterized in that, also comprise circulatory mediator temperature-adjusting device, be arranged between described First Heat Exchanger (2) and the second heat exchanger (3), to regulate the temperature of described annular channel Inner eycle medium.
8. industrial waste water disposal device as claimed in claim 7, it is characterized in that, described circulatory mediator temperature-adjusting device comprises first-class absorption type heat pump (6) and the 3rd pump (7), the heat source water entrance (A of described first-class absorption type heat pump (6)
in) be communicated with the media outlet of the second medium runner (22) of described First Heat Exchanger (2), its heat source water outlet (A
out) be communicated with the medium inlet of the second medium runner (22) of described First Heat Exchanger (2), its hot water inlet (B
in) be communicated with the media outlet of described second heat exchanger (3), its hot water outlet (B
out) be communicated with the medium inlet of described second pump (5), its steam inlet (H
in) and solidifying water out (H
out) for being communicated with outside heating plant, described 3rd pump (7) is arranged at the media outlet of the second medium runner (22) of described First Heat Exchanger (2) and described hot water inlet (B
in) between.
9. industrial waste water disposal device as claimed in claim 7, it is characterized in that, described circulatory mediator temperature-adjusting device comprises second-kind absorption-type heat pump (8) and the 4th pump (9), the heat source water entrance (D of described second-kind absorption-type heat pump (8)
in) be communicated with the media outlet of the second medium runner (22) of described First Heat Exchanger (2), its heat source water outlet (D
out) be communicated with the medium inlet of the second medium runner (22) of described First Heat Exchanger (2), its hot water inlet (E
in) be communicated with the media outlet of described second heat exchanger (3), its hot water outlet (E
out) be communicated with the medium inlet of described second pump (5), its cooling water inlet (C
in) and coolant outlet (C
out) for being communicated with external refrigeration device, described 4th pump (9) is arranged at the media outlet of the second medium runner (22) of described First Heat Exchanger (2) and described hot water inlet (E
in) between.
10. industrial waste water disposal device as claimed in claim 7, it is characterized in that, described circulatory mediator temperature-adjusting device comprises auxiliary cooling tower (G) and the 3rd heat exchanger (I), described 3rd heat exchanger (I) to be installed in described auxiliary cooling tower (G) and to be positioned at spray pipeline (13) below, and its medium inlet is communicated with described second heat exchanger (3), and its media outlet is communicated with described First Heat Exchanger (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420400283.4U CN204064029U (en) | 2014-07-18 | 2014-07-18 | A kind of industrial waste water disposal device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420400283.4U CN204064029U (en) | 2014-07-18 | 2014-07-18 | A kind of industrial waste water disposal device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204064029U true CN204064029U (en) | 2014-12-31 |
Family
ID=52205520
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420400283.4U Withdrawn - After Issue CN204064029U (en) | 2014-07-18 | 2014-07-18 | A kind of industrial waste water disposal device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204064029U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104110975A (en) * | 2014-07-18 | 2014-10-22 | 烟台荏原空调设备有限公司 | Industrial wastewater treatment device |
| CN108751559A (en) * | 2018-08-13 | 2018-11-06 | 浏阳市亿臻燃油有限公司 | A kind of industrial wastewater regeneration cycle processing method and its system |
-
2014
- 2014-07-18 CN CN201420400283.4U patent/CN204064029U/en not_active Withdrawn - After Issue
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104110975A (en) * | 2014-07-18 | 2014-10-22 | 烟台荏原空调设备有限公司 | Industrial wastewater treatment device |
| CN104110975B (en) * | 2014-07-18 | 2016-07-13 | 烟台荏原空调设备有限公司 | A kind of industrial waste water disposal device |
| CN108751559A (en) * | 2018-08-13 | 2018-11-06 | 浏阳市亿臻燃油有限公司 | A kind of industrial wastewater regeneration cycle processing method and its system |
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