CN203269606U - Evaporation system - Google Patents
Evaporation system Download PDFInfo
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- CN203269606U CN203269606U CN 201320283734 CN201320283734U CN203269606U CN 203269606 U CN203269606 U CN 203269606U CN 201320283734 CN201320283734 CN 201320283734 CN 201320283734 U CN201320283734 U CN 201320283734U CN 203269606 U CN203269606 U CN 203269606U
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- evaporator room
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Abstract
The utility model provides an evaporation system. The evaporation system comprises an evaporation chamber, a condensation chamber, a fan unit, a water supply pipe and a bypass pipe, wherein the evaporation chamber is provided with a first inlet and a first outlet; the condensation chamber is provided with a second inlet, a second outlet and a condensation pipe arranged between the second inlet and the second outlet; the second inlet is communicated with the first outlet; the second outlet is communicated with the first inlet; the fan unit leads the steam in the evaporation chamber to the condensation chamber and is arranged between the first outlet and the second inlet; the water supply pipe supplies fluid to be evaporated to the evaporation chamber and is arranged outside the evaporation chamber; the bypass pipe is used for the steam in the evaporation chamber to flow through and is communicated with the evaporation chamber to form a circulation loop; and the bypass pipe is arranged outside the evaporation chamber to form a heat conducting pipe carrying out heat exchange with the fluid to be evaporated in the water supply pipe. The evaporation system has the beneficial effects that the evaporation system improves the treatment efficiency of the fluid to be evaporated; and moreover, as the bypass pipe is arranged outside the evaporation chamber, the waste heat is utilized to improve the evaporation capacity of the fluid to be evaporated.
Description
Technical field
The utility model relates to a kind of vapo(u)rization system.
Background technology
For the sensu lato strong brine that comprises magnesium ion, calcium ion, iron ion, sodium-chlor in prior art, especially in prior art, specific conductivity is that the above effective treating method of strong brine of 60000 μ s/cm is to use the multiple-effect high-temperature evaporation unit, make processed water surpass boiling point, become steam raising and go out.Its shortcoming is that power consumption is large, and efficient is low.
The utility model content
For the problem that exists in correlation technique, the purpose of this utility model is to provide a kind of vapo(u)rization system, can effectively process fluid to be evaporated, and can be beneficial to waste heat (produce in evaporator room in the vapo(u)rization system working process steam institute heat content) and improve the steam capability for the treatment of evaporative fluid.
For achieving the above object, the utility model provides a kind of vapo(u)rization system to comprise: evaporator room has the first entrance and the first outlet; Condensing chamber has the second entrance, the second outlet, is arranged on the prolong between the second entrance and the second outlet, and wherein the second entrance is communicated with the first outlet, and the second outlet is communicated with the first entrance; The blower fan group of steam flow condensing chamber in the guiding evaporator room is located between the first outlet and the second entrance, and the water-supply pipe of fluid to be evaporated is provided to evaporator room, is located at outside evaporator room; For the bypass pipe of vapour stream warp in evaporator room, be communicated with the formation circulation loop with evaporator room; Wherein, bypass pipe is located at outside evaporator room, the heat pipe of fluid thermal exchange to be evaporated in formation and water-supply pipe.
Preferably, water-supply pipe is wrapped on bypass pipe.
Preferably, also comprise the pipeline section that wherein is provided with heating unit, a pipe port of pipeline section is communicated with the second outlet, and another pipe port is communicated with the first entrance.
Preferably, heating unit is warm air curtain.
Preferably, be provided with a plurality of nozzles in evaporator room, nozzle is communicated with the water outlet of water-supply pipe, and nozzle is between the first entrance and the first outlet.
Preferably, also comprise: padding support frame and be placed on filler on filler support all is arranged in evaporator room and between nozzle and the first entrance, padding support frame has the through hole that communicates with the first entrance.
Preferably, in evaporator room, be provided with the spiral conveyer of the below that is positioned at padding support frame, the discharge port of spiral conveyer stretches out from evaporator room.
Preferably, evaporator room, condensing chamber material are plastics.
Preferably, the material of evaporator room, condensing chamber, pipeline section is plastics.
Than prior art, the beneficial effects of the utility model are:
1. in the utility model vapo(u)rization system, condensing chamber the second entrance is communicated with evaporator room the first outlet, and condensing chamber the second outlet is communicated with evaporator room the first entrance, thereby can provide carry out the circulation loop of condensation from steam in evaporator room, improve the processing efficiency of fluid to be evaporated, effectively processed fluid to be evaporated; Further because bypass pipe is arranged on the evaporator room outside, for vapour stream warp in evaporator room, fluid generation heat exchange to be evaporated in steam and water-supply pipe in bypass pipe, in evaporator room, steam is raised the temperature of fluid to be evaporated before sending into evaporator room thereby utilize, and namely the utility model can be beneficial to the steam capability that waste heat (produce in evaporator room in the vapo(u)rization system working process steam institute heat content) improves fluid to be evaporated.
2. evaporator room is communicated with condensing chamber, consists of carry out the circulation loop of condensation from steam in evaporator room, has realized like this treating the circular treatment of evaporative fluid.
3. be communicated with the pipeline section with heating unit between the first entrance of second of condensing chamber the outlet and condensing chamber, this has accelerated the velocity of evaporation of fluid to be evaporated.
4. the filler in evaporator room has increased the evaporation area of fluid to be evaporated, thereby has improved vaporization efficiency, and the requirement to filler in the utility model is the evaporation area that can increase fluid to be evaporated, and not by this flow-induced corrosion to be evaporated.
When processing object of the present utility model be that the specific conductivity of 40-90 ℃ is when being strong brine more than 60000 μ s/cm, because this strong brine can produce water vapor at 40-90 ℃, so the Working environment that the utility model provides for strong brine can be over 90 ℃, in this case, evaporator room in vapo(u)rization system, condensing chamber, pipeline section etc. are all thought plastics, thereby the utility model cost and weight are lighter.Especially, when the processing object was above-mentioned strong brine, the pipeline section with heating unit can improve extra heat, makes strong brine constantly be evaporated, and this sample system finally can be processed into strong brine solid residue (can be referred to as dried salt).Therefore, it is better that the utility model makes the strong brine treatment effect.
Description of drawings
Fig. 1 is the schematic diagram of the utility model vapo(u)rization system.
Embodiment
Be described below in conjunction with 1 pair of the utility model embodiment of accompanying drawing.
Vapo(u)rization system comprises: evaporator room 1, condensing chamber 2, water-supply pipe 15 and bypass pipe 14, wherein, evaporator room has the first entrance 6 and the first outlet 3.Condensing chamber 2 has the second entrance 4 and the second outlet 5, the first outlet 3 of evaporator room is communicated with the second entrance 4 of condensing chamber 2, the second outlet 5 of condensing chamber 2 is communicated with the first entrance 6 of evaporator room, and, be arranged in condensing chamber 2 between second outlet the 5 and second entrance 4 and be provided with prolong.Water-supply pipe 15 provides fluid to be evaporated in the evaporator room outside to evaporator room, is provided with bypass pipe, and bypass pipe is communicated with the formation circulation loop with evaporator room, vapour stream warp in bypass pipe confession evaporator room, and carry out heat exchange with fluid to be evaporated in water-supply pipe 15.Simultaneously, can flow to condensing chamber 2 in order to guide the steam in evaporator room, blower fan group 13 is set in the first outlet between the 3 and second entrance 4, make from the steam of evaporator room can be recycled condensation in condensing chamber.Above-mentioned the first outlet 3 is communicated with the second entrance 4, the second outlet 5 is communicated with formation to carry out another circulation loop of condensation from steam in evaporator room with the first entrance 6, in order to distinguish with the circulation loop of above-mentioned bypass pipe, here the circulation loop that the first outlet 3 is communicated with the second entrance 4, the second outlet 5 is communicated with formation with the first entrance 6 is referred to as the first circulation loop, is referred to as the second circulation loop and bypass pipe is communicated with the formation circulation loop with evaporator room.
Should be appreciated that, clearly can provide fluid to be evaporated by water-supply pipe 15 to evaporator room by pump 11.In addition, above-mentioned fluid to be evaporated strong brine preferably.For convenience of description, the below will be take strong brine as example, and for example temperature is that 40-90 ℃ of specific conductivity is the above strong brines of 60000 μ s/cm.Obviously the utility model vapo(u)rization system can be low temperature closed loop vapo(u)rization system, and when the processing object was above-mentioned strong brine, its Working environment that passes through for strong brine can be over 90 ℃.
Should be appreciated that, the position that above-mentioned blower fan group 13 arranges is only preferred mode, can also be arranged on any position that can guide the steam flow condensing chamber 2 in evaporator room of the first circulation loop.The above-mentioned steam of mentioning includes but not limited to that 40-90 ℃ of specific conductivity is the water vapor of above strong brine self band of 60000 μ s/cm.Above-mentioned strong brine comprises one or more in magnesium ion, calcium ion, iron ion, sodium-chlor at least.
Above-mentioned system can be that 40-90 ℃ and specific conductivity are water effective ground evaporation in the above strong brine of 60000 μ s/cm with the temperature that enters evaporator room, and the mode with the evaporation of low temperature closed loop has improved the ability that strong brine is processed like this.Further because bypass pipe is arranged on the evaporator room outside, for vapour stream warp in evaporator room, fluid generation heat exchange to be evaporated in steam and water-supply pipe in bypass pipe, in evaporator room, steam is raised the temperature of fluid to be evaporated before sending into evaporator room thereby utilize, and namely the utility model can be beneficial to the steam capability that waste heat (produce in evaporator room in the vapo(u)rization system working process steam institute heat content) improves fluid to be evaporated.
Further, the quantity of evaporator room is at least one, preferably four (all not illustrating in accompanying drawing), and the first outlet 3 of each evaporator room all is communicated with the second entrance 4 of condensing chamber 2, the second outlet 5 of condensing chamber 2 is communicated with the first entrance 6 of each evaporator room, here, the quantity of condensing chamber 2 second outlet the 5 and second entrances 4 at least respectively has one, concrete quantity does not limit, its can for can according to above-mentioned the first outlet 3 and the second entrance 4, the second outlet 5 with the first entrance 6 is communicated with any individual.Should be appreciated that, as shown in Figure 1, the first outlet 3 of each evaporator room can be same mouthful.When being a plurality of, many water-supply pipes can be set when evaporator room, the bypass pipe heat exchange that each water-supply pipe and evaporator room are outer.
For convenience's sake, below to the description of evaporator room, all be as the criterion with one, the structure of all the other each evaporator rooms of any amount is all identical with evaporator room described below.
Above-mentioned bypass pipe novel according to this use and the strong brine heat exchange in water-supply pipe, its implementation is that water-supply pipe is wrapped on bypass pipe.Should be appreciated that this is a kind of preferred mode, other modes that can realize heat exchange are equally applicable to the utility model, for example bypass pipe is spaced apart with water-supply pipe and need not directly contact, as long as spacing distance can make fluid generation heat exchange in fluid and water-supply pipe in bypass pipe.
Vapo(u)rization system of the present utility model also comprises pipeline section 7, and a port of pipeline section 7 is communicated with the second outlet 5, and another port is communicated with the first entrance 6, and is provided with heating unit on pipeline section 7.In a preferred embodiment, second outlet the 5 and first entrance 6 is realized being communicated with by pipeline section 7, the heating unit of pipeline section 7 preferably be warm air curtain, preferred Heating temperature is for just making the temperature of strong brine generation water vapor in evaporator room, for example be preferably 40-90 ℃ or 60-90 ℃, but can be over 90 ℃.Obviously be appreciated that under the situation of the pipeline section 7 with heating unit, in evaporator room, strong brine can continue to produce water vapor, thereby the utility model vapo(u)rization system can finally make the strong brine in evaporator room crystallize at last dried salt.
Further, be provided with nozzle 8 in the evaporator room 1 of the utility model vapo(u)rization system, nozzle 8 is between the first entrance 6 and the first outlet 3, and above-mentioned water-supply pipe, is communicated with the water outlet of water-supply pipe and realizes for strong brine to evaporator room with nozzle.Can also use pump 11 as above-mentioned, pump is that 40-90 ℃ and specific conductivity are that strong brine more than 60000 μ s/cm is carried by water-supply pipe with temperature, sprays into evaporator room 1 by nozzle.Certainly using nozzle is only optimal way, as long as can carry strong brine to evaporator room, also can without nozzle.Further preferably, all nozzles are that plastics are made, and certainly, these plastics should be able to anti-strong brine corrosion.
Further, above-mentioned dried salt can transport evaporator room 1 by spiral conveyer 12, and spiral conveyer 12 is arranged in evaporator room, be positioned at padding support frame 10 belows, and the discharge port of spiral conveyer 12 stretches out from evaporator room 1.
in a preferred embodiment, processing object when the utility model is: temperature is 40-90 ℃, and when specific conductivity is the above strong brine of 60000 μ s/cm, because this strong brine namely produces water vapor at 40-90 ℃, so the working temperature of this vapo(u)rization system can not surpass 90 ℃ (even have under situation with the pipeline section of heating unit, heating unit can not be heated to the air-flow (or mixture of air-flow and steam) of the heating unit of flowing through over 90 ℃ yet) just strong brine can be processed into dried salt, therefore, evaporator room 1, condensing chamber 2, the material of pipeline section 7 all can be plastics, this just makes the utility model vapo(u)rization system cost, lighten.Should be appreciated that, plastics are a kind of preferred materials, are not limited to the utility model, and other materials goes for the utility model equally, but should guarantee at least to have the erosion resistance to the above-mentioned strong brine of the utility model.
The descriptions such as the position relationship of the nozzle 8 that above-mentioned evaporator room comprises, filler 9, padding support frame 10, spiral conveyer 12 etc. and material are applicable to each in the evaporator room of any amount.
has above-mentioned filler with the utility model vapo(u)rization system, and above-mentioned pipeline section with heating unit is example, processing object is that 40-90 ℃ of specific conductivity is that the above strong brine of 60000 μ s/cm is example, the working process that the utility model vapo(u)rization system processing strong brine is described is: water-supply pipe supplies described strong brine to the nozzle 8 in evaporator room, strong brine is attached to the evaporation area that makes strong brine on filler and becomes large, the air-flow that the water vapor that strong brine produces produces by blower fan group 13, flow to the second entrance from the first outlet, the final condensing chamber that flows into, cooling formation water of condensation through the prolong in condensing chamber, because the blower fan group is arranged between the first outlet and the second entrance, produce air-flow guiding steam and flow into condensing chamber from evaporator room, same, the air-flow that produces also can flow into evaporator room the first entrance from the second outlet of condensing chamber, and, the heating of heating unit air-flow can be subject to pipeline section the process that flows into evaporator room the first entrance from the second outlet in, air-flow after heating passes the through hole of padding support frame, the flow direction is mixed with the filler of strong brine, further promote the evaporation of strong brine, produce water vapor, and enter condensing chamber in this guiding by the blower fan group, with this circulating and evaporating, condensation, thereby realize the processing to strong brine.When the utility model vapo(u)rization system continuous service, it is dried salt that strong brine can be processed into last crystallization, and dried salt can be discharged with spiral conveyer.Utilize the process of strong brine in the waste-heat water-supply pipe as follows: the water vapor that in evaporator room, strong brine produces by bypass pipe can with water-supply pipe in strong brine carry out heat exchange, due to the temperature of steam in the bypass pipe temperature higher than strong brine in water-supply pipe, so steam strong brine release of heat in the water-supply pipe in bypass pipe.
In addition, the refrigerant of prolong in the utility model condensing chamber, can by be located at evaporator room and condensing chamber the outside compressor (not shown) provide.Above-mentioned pump 11 is arranged on outside evaporator room and condensing chamber.
As a kind of optimal way, except the 40-90 ℃ of temperature and the above specific conductivity condition of 60000 μ s/cm that satisfy above-mentioned definition, strong brine can be except water also, only contain magnesium ion, calcium ion, iron ion, sodium-chlor, no matter and the per-cent between each component how, gets final product so long as can evaporate at 40-90 ℃.
Fig. 1 also shows valve 15 and 17 in addition, and when valve 17 shut-off valves 15 were opened, pump 11 made strong brine circulate between evaporator room and strong brine container (not shown).When valve 17 is opened, can strong brine be supplied with from the outside strong brine container.
The above is only preferred embodiment of the present utility model, is not limited to the utility model, and for a person skilled in the art, the utility model can have various modifications and variations.All within spirit of the present utility model and principle, any modification of doing, be equal to replacement, improvement etc., within all should being included in protection domain of the present utility model.
Claims (9)
1. a vapo(u)rization system, is characterized in that, comprising:
Evaporator room has the first entrance and the first outlet;
Condensing chamber has the second entrance, the second outlet, is arranged on the prolong between described the second entrance and described the second outlet, and wherein said the second entrance is communicated with described the first outlet, and described the second outlet is communicated with described the first entrance;
Guide the blower fan group of the described condensing chamber of steam flow in described evaporator room, be located between described the first outlet and the second entrance,
The water-supply pipe of fluid to be evaporated is provided to described evaporator room, is located at outside described evaporator room;
For the bypass pipe of vapour stream warp in described evaporator room, be communicated with the formation circulation loop with described evaporator room;
Wherein, described bypass pipe is located at outside described evaporator room, the heat pipe of fluid thermal exchange to be evaporated in formation and described water-supply pipe.
2. vapo(u)rization system according to claim 1, is characterized in that,
Described water-supply pipe is wrapped on described bypass pipe.
3. vapo(u)rization system according to claim 1 and 2, is characterized in that,
Also comprise the pipeline section that wherein is provided with heating unit, a pipe port of described pipeline section is communicated with described the second outlet, and another pipe port is communicated with described the first entrance.
4. vapo(u)rization system according to claim 3, is characterized in that,
Described heating unit is warm air curtain.
5. the described vapo(u)rization system of any one according to claim 1-2,4, is characterized in that,
Be provided with a plurality of nozzles in evaporator room, described nozzle is communicated with the water outlet of described water-supply pipe, and described nozzle is between described the first entrance and the first outlet.
6. vapo(u)rization system according to claim 5, is characterized in that,
Also comprise: padding support frame and be placed on filler on described filler support all is arranged in described evaporator room and between described nozzle and the first entrance, described padding support frame has the through hole that communicates with described the first entrance.
7. vapo(u)rization system according to claim 6, is characterized in that,
In described evaporator room, be provided with the spiral conveyer of the below that is positioned at described padding support frame, the discharge port of described spiral conveyer stretches out from described evaporator room.
8. according to claim 1-2,4, the described vapo(u)rization system of any one in 6-7, it is characterized in that,
Described evaporator room, condensing chamber material are plastics.
9. vapo(u)rization system according to claim 3, is characterized in that,
The material of described evaporator room, condensing chamber, pipeline section is plastics.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320283734 CN203269606U (en) | 2013-05-22 | 2013-05-22 | Evaporation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320283734 CN203269606U (en) | 2013-05-22 | 2013-05-22 | Evaporation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203269606U true CN203269606U (en) | 2013-11-06 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320283734 Expired - Lifetime CN203269606U (en) | 2013-05-22 | 2013-05-22 | Evaporation system |
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| CN (1) | CN203269606U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109195639A (en) * | 2016-04-27 | 2019-01-11 | 利乐拉瓦尔集团及财务有限公司 | The method of hydrogen peroxide vaporising device and evaporation hydrogen peroxide |
-
2013
- 2013-05-22 CN CN 201320283734 patent/CN203269606U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109195639A (en) * | 2016-04-27 | 2019-01-11 | 利乐拉瓦尔集团及财务有限公司 | The method of hydrogen peroxide vaporising device and evaporation hydrogen peroxide |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20131106 |
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| CX01 | Expiry of patent term |