CN204643888U - Water treatment low-temp low-pressure plate type evaporating apparatus - Google Patents
Water treatment low-temp low-pressure plate type evaporating apparatus Download PDFInfo
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- CN204643888U CN204643888U CN201520116678.6U CN201520116678U CN204643888U CN 204643888 U CN204643888 U CN 204643888U CN 201520116678 U CN201520116678 U CN 201520116678U CN 204643888 U CN204643888 U CN 204643888U
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Abstract
The utility model relates to water treatment low-temp low-pressure plate type evaporating apparatus, comprise housing, water circulating pump, many group plate-type heat exchangers are disposed in series in described housing, at each plate-type heat exchanger adjacent, in described housing, also arrange vaporizer, base of evaporator also arranges ceramic raw material strainer; Also well heater is arranged in described housing; Also air intlet pump and air vout is arranged respectively outward at described housing.The utility model adopts integral structure, does not need steam and compressor, have floor space little, be easy to safeguard, do not need civil engineering, operation energy consumption is lower, low noisiness, the advantages such as fully-automatic intelligent control, power consumption than traditional shell and tube evaporator and MVR vapo(u)rization system little by 80%, overall cost of investment reduces by more than 30%.It utilizes plate-type heat exchanger to make one-piece construction very compact, and under the identical condition of evaporation quantity, institute takes up space as 1/3 to 1/4 of tube-type down-flow evaporator, is highly 1/10 of tube-type down-flow evaporator, easy accessibility, and equipment heat interchanging area adjusts flexible.
Description
Technical field
The utility model relates to water treating equipment, particularly relates to water treatment low-temp low-pressure plate type evaporating apparatus.
Background technology
High slat-containing wastewater refers to the waste water of total saliferous massfraction at least 1%, and it is mainly from collection and the processing of chemical plant and petroleum and natural gas, and this waste water is usually containing many kinds of substance (comprising salt, oil, organic heavy metal and radioactive substance).High-concentration waste water refers to the high density of chemical oxygen demand cod higher than 2000mg/L, even up to the high pollution waste water of 5-8 ten thousand mg/L, such as Wastewater from Pig Farm, electroplating wastewater, printing ink wastewater etc., current high slat-containing wastewater and high-concentration waste water are one of the most unmanageable domestic waste water, above-mentioned useless water problem seriously restricts the development of industry and enterprise, and how to process is a lot of experts and scholars, the emphasis of engineering technical personnel's further investigation, it is mainly concerned with materializing strategy and high saliferous biochemical treatment two aspects, the high saliferous of tradition and high concentration wastewater treatment adopt vapo(u)rization system and the MVR evaporation technique of shell and tube pump circulation substantially, but this evaporation technique needs to adopt vaporizer, its power consumption is large, equipment material corrosion resistance is poor, steam consumption is large, water pump and compressor apparatus cost high, heat transfer efficiencies is low, bulky, cost is high, serious restriction its at high saliferous, application in high concentration wastewater treatment.
Utility model content
The applicant is for above-mentioned existing issue, be studied improvement, water treatment low-temp low-pressure plate type evaporating apparatus is provided, the integrated overall plastic structure of this structure vaporizer, do not need steam and compressor, its have floor space little, be easy to safeguard, do not need civil engineering, operation energy consumption is lower, low noisiness, corrosion-resistant, fully-automatic intelligent controls, the advantage of compact construction, easy accessibility.
The technical scheme that the utility model adopts is as follows:
Water treatment low-temp low-pressure plate type evaporating apparatus, comprises housing, and many group plate-type heat exchangers are disposed in series in described housing, at each plate-type heat exchanger adjacent, in described housing, also arrange vaporizer and well heater respectively; Also air intlet pump and air vout is arranged respectively outward at described housing; Pure water pipe is discharged after discharging dense water pipe, process also arrange water circulating pump, water-in, water cycle reprocessing Guan Yuanshui water inlet pipe and process in described housing after.
Its further technical scheme is:
Each group of plate-type heat exchanger all comprises two male and fomale(M&F) passages, the multiple asperities replaced continuously of each male and fomale(M&F) passage composition, and each asperities is separated by pressure rolling straight line;
Described male and fomale(M&F) passage comprises multiple recess of replacing continuously and protuberance, two adjacent each other recesses and protuberance are connected by a rhombus, described rhombus forms by by two coplanar trilaterals of isosceles, between each neighboring diamonds centered by longitudinal seamed edge symmetrical two isosceles trapezoids;
Described plate-type heat exchanger adopts any one material extrusion and blow molding in highstrenghtpiston, pottery, stainless steel or polymerizable material;
Described housing adopts high strength plastic materials to make;
Described vaporizer adopts highstrenghtpiston's structure and ceramic raw material strainer composition;
One end of described water circulating pump is connected with one end of water treatment recirculation pipe by source water water inlet pipe, and the other end of described water treatment recirculation pipe is communicated with described housing, and the other end of described water circulating pump is communicated with water-in by water treatment recirculation pipe; Discharge pure water pipe after discharging dense water pipe, process after described water pump, water-in, source water water inlet pipe and process and all adopt highstrenghtpiston's structure.
The beneficial effects of the utility model are as follows:
The utility model have floor space little, be easy to safeguard, do not need the advantage of civil engineering, power consumption is less than traditional shell and tube evaporator by 80%, and overall cost of investment reduces by more than 30%.It utilizes plate-type heat exchanger to make one-piece construction very compact, under the condition that evaporation quantity is identical, take up space as 1/3 to 1/4 of tube-type down-flow evaporator, it is highly 1/10 of tube-type down-flow evaporator, its maintenance only needs loosening fasteners can touch plate-type heat exchanger in former spatial dimension, easy accessibility, the adjustment of equipment heat interchanging area flexibly, that in plate-type heat exchanger, the size of each plate is minimum is 0.03 ㎡, maximumly reach 4 more than ㎡, the most I of heat interchanging area of every platform equipment reaches 0.5 ㎡, maximumly reaches 1900 more than ㎡.
Suitable heat-transfer effect and capacity can be obtained by the number or changing process that regulate heat exchanger plates, for user provides the possibility changing treatment capacity at any time and change energy saving or increase New function, because compact construction volume is little, the outer surface area of vaporizer is little, therefore thermosteresis is little, the pressure-losses is few, under the condition of identical heat transfer coefficient, plate-type heat exchanger is by reasonably selecting flow velocity, the pressure-losses can be controlled in the scope of 1/3 of tube-type down-flow evaporator, safe and reliable, telltale hole can be increased in addition, if leak, can be got rid of at vaporizer outside, prevent steam and mixing of materials, play again safety alarm effect, realize low-temp low-pressure Multi-effect plate type evaporation concentration system function, power consumption is less than traditional shell and tube evaporator by 80%, overall cost of investment reduces by more than 30%.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the structural representation of plate-type heat exchanger male and fomale(M&F) passage.
Fig. 3 is the structural representation of plate-type heat exchanger in the utility model.
Wherein: 1, housing; 2, well heater; 201, heater outlet; 3, plate-type heat exchanger; 4, vaporizer; 5, air intlet pump; 6, air vout; 7, water-in; 8, water treatment recirculation pipe; 9, water circulating pump; 10, dense water pipe is discharged after process; 11, pure water pipe is discharged after process; 12, source water water inlet pipe.
Embodiment
Below in conjunction with accompanying drawing, embodiment of the present utility model is described.
As shown in Figure 1, water treatment low-temp low-pressure plate type evaporating apparatus comprises housing 1, and housing 1 adopts high strength plastic materials to make.Multiple plate-type heat exchanger 3 is disposed in series in housing 1, at each plate-type heat exchanger 3 adjacent, in housing 1, also arranges vaporizer 4.In housing 1, also arrange well heater 2, heater outlet 201 is also set in the side of well heater 2.Outside housing 1, also arrange air intlet pump 5 and air vout 6 respectively, this air intlet pump 5 is connected with housing 1.As shown in Figure 2 and Figure 3, each plate-type heat exchanger 3 all comprises two male and fomale(M&F) passages, and the multiple asperities replaced continuously of each male and fomale(M&F) passage composition, each asperities by pressure rolling straight line 33 separately.Above-mentioned male and fomale(M&F) passage comprises multiple recess 31 of replacing continuously and protuberance 32, two adjacent each other recesses 31 and protuberance 32 are connected by a rhombus 34, rhombus 34 is made up of two coplanar trilaterals of isosceles, between each neighboring diamonds 34 centered by longitudinal seamed edge 35 symmetrical two isosceles trapezoids 36.Above-mentioned plate-type heat exchanger 3 adopts plastics, also can adopt any one material extrusion and blow molding in pottery, high-strength stainless steel or polymerizable material.
As shown in Figure 1, one end of above-mentioned water circulating pump 9 is connected with one end of water treatment recirculation pipe 8 by source water water inlet pipe 12, and the other end of water treatment recirculation pipe 8 is communicated with housing 1, and the other end of water circulating pump 9 is communicated with water-in 7 by water treatment recirculation pipe 8; Discharge pure water pipe 11 after discharging dense water pipe 10, process after water circulating pump 9, water-in 7, source water water inlet pipe 12 and process and all adopt highstrenghtpiston's structure.
Specific works process of the present invention is as follows:
As shown in Figure 1, waste water is by source water water inlet pipe 12, water circulating pump 9, water treatment recirculation pipe 8 enters water-in 7 and inputs to the plate-type heat exchanger 3 in housing 1, upwards flow out into well heater 2 from the top of plate-type heat exchanger 3 under waste water has and heat, waste water is heated to 85 DEG C needed for vaporizer 4, well heater 2 is immerseable electric heater, water can be heated to 90 ~ 93 ° by this immerseable electric heater, the thermal wastewater reaching temperature flows out into vaporizer 4 from heater outlet 201, vaporizer 4 adopts plastics and ceramic raw material to make, while thermal wastewater enters vaporizer 4, air intlet pump 5 suction outside air enters the vaporizer 4 in housing 1, vaporizer 4 is utilized to optimize surface in contact between air and thermal wastewater, bottom air Injection to current, saturated wet air is formed after air heats, simultaneously the moisture separating treatment 90% needed in all kinds of high-concentration sewage to be processed or high slat-containing wastewater is purified waste water effect by its steam produced, only the concentrated water drainage of surplus 10% goes out, the waste water that art breading does not complete continues to flow in water treatment recirculation pipe 8 and processes.Saturated moist air was passed in plate-type heat exchanger 3 and condenses after multiple recess 31 and protuberance 32 before pre-thermal wastewater (75 °) enters well heater 2, and finally form clear water and flow out housing 1, the air of water content does not flow out from air vout 6 in addition, circulates with this.
It is little that the utility model has floor space, be easy to safeguard, do not need the advantage of civil engineering, it utilizes plate-type heat exchanger to make one-piece construction very compact, under the condition that evaporation quantity is identical, take up space as 1/3 to 1/4 of tube-type down-flow evaporator, it is highly 1/10 of tube-type down-flow evaporator, its maintenance only needs loosening fasteners can touch plate-type heat exchanger in former spatial dimension, easy accessibility, the adjustment of equipment heat interchanging area flexibly, that in plate-type heat exchanger, the size of each plate is minimum is 0.03 ㎡, maximumly reach 4 more than ㎡, the most I of heat interchanging area of every platform equipment reaches 0.5 ㎡, maximumly reach 1900 more than ㎡.Suitable heat-transfer effect and capacity can be obtained by the number or changing process that regulate heat exchanger plates, for user provides the possibility changing treatment capacity at any time and change energy saving or increase New function, because compact construction volume is little, the outer surface area of vaporizer is little, therefore thermosteresis is little, the pressure-losses is few, under the condition of identical heat transfer coefficient, plate-type heat exchanger is by reasonably selecting flow velocity, the pressure-losses can be controlled in the scope of 1/3 of tube-type down-flow evaporator, safe and reliable, telltale hole can be increased in addition, if leak, can be got rid of at vaporizer outside, prevent steam and mixing of materials, play again safety alarm effect, realize low-temp low-pressure Multi-effect plate type evaporation concentration system function, water treatment low-temp low-pressure plate type evaporating apparatus possesses corrosion-resistant, fully-automatic intelligent controls, power consumption is less than traditional shell and tube evaporator by 80%, overall cost of investment reduces by more than 30%.
More than describing is to explanation of the present utility model, and be not the restriction to utility model, the utility model limited range is see claim, and when without prejudice to basic structure of the present utility model, the utility model can do any type of amendment.
Claims (7)
1. water treatment low-temp low-pressure plate type evaporating apparatus, it is characterized in that: comprise housing (1), organize plate-type heat exchanger (3) is disposed in series in described housing (1) more, at each plate-type heat exchanger (3) adjacent, in described housing (1), also arranges vaporizer (4) and well heater (2) respectively; Also air intlet pump (5) and air vout (6) is arranged respectively outward at described housing (1); Pure water pipe (11) is discharged after discharging dense water pipe (10), process also arrange water circulating pump (9), water-in (7), water treatment recirculation pipe (8), source water water inlet pipe (12) and process in described housing (1) after.
2. water treatment low-temp low-pressure plate type evaporating apparatus as claimed in claim 1, it is characterized in that: respectively organize plate-type heat exchanger (3) and all comprise two male and fomale(M&F) passages, the multiple asperities replaced continuously of each male and fomale(M&F) passage composition, each asperities by pressure rolling straight line (33) separately.
3. water treatment low-temp low-pressure plate type evaporating apparatus as claimed in claim 2, it is characterized in that: described male and fomale(M&F) passage comprises multiple recess (31) of replacing continuously and protuberance (32), two adjacent each other recesses (31) and protuberance (32) are connected by a rhombus (34), described rhombus (34) forms by by two coplanar trilaterals of isosceles, between each neighboring diamonds (34) centered by longitudinal seamed edge (35) symmetrical two isosceles trapezoids (36).
4. water treatment low-temp low-pressure plate type evaporating apparatus as claimed in claim 1, is characterized in that: described plate-type heat exchanger (3) adopts any one material extrusion and blow molding in highstrenghtpiston, pottery, stainless steel or polymerizable material.
5. water treatment low-temp low-pressure plate type evaporating apparatus as claimed in claim 1, is characterized in that: described housing (1) adopts high strength plastic materials to make.
6. water treatment low-temp low-pressure plate type evaporating apparatus as claimed in claim 1, is characterized in that: described vaporizer (4) adopts highstrenghtpiston's structure and ceramic raw material strainer composition.
7. water treatment low-temp low-pressure plate type evaporating apparatus as claimed in claim 1, it is characterized in that: one end of described water circulating pump (9) is connected with one end of water treatment recirculation pipe (8) by source water water inlet pipe (12), the other end of described water treatment recirculation pipe (8) is communicated with described housing (1), and the other end of described water circulating pump (9) is communicated with water-in (7) by water treatment recirculation pipe (8); Discharge pure water pipe (11) after discharging dense water pipe (10), process after described water pump (9), water-in (7), source water water inlet pipe (12) and process and all adopt highstrenghtpiston's structure.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520116678.6U CN204643888U (en) | 2015-02-26 | 2015-02-26 | Water treatment low-temp low-pressure plate type evaporating apparatus |
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| CN201520116678.6U CN204643888U (en) | 2015-02-26 | 2015-02-26 | Water treatment low-temp low-pressure plate type evaporating apparatus |
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| CN204643888U true CN204643888U (en) | 2015-09-16 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104692477A (en) * | 2015-02-26 | 2015-06-10 | 江苏新纪元环保有限公司 | Water treatment low-temperature low-pressure evaporator of integrated structure |
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2015
- 2015-02-26 CN CN201520116678.6U patent/CN204643888U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104692477A (en) * | 2015-02-26 | 2015-06-10 | 江苏新纪元环保有限公司 | Water treatment low-temperature low-pressure evaporator of integrated structure |
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