CN204543580U - A kind of solar energy evaporation concentration device - Google Patents
A kind of solar energy evaporation concentration device Download PDFInfo
- Publication number
- CN204543580U CN204543580U CN201520056331.7U CN201520056331U CN204543580U CN 204543580 U CN204543580 U CN 204543580U CN 201520056331 U CN201520056331 U CN 201520056331U CN 204543580 U CN204543580 U CN 204543580U
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- solar energy
- evaporimeter
- pipe
- evaporator
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- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a kind of solar energy evaporation concentration device.Comprise charging basket, solar energy heat collection pipe and evaporimeter, charging basket is communicated with by the feed pipe being provided with feed pump with the feeding mouth of solar energy heat collection pipe, the discharging opening of solar energy heat collection pipe is communicated with by discharge nozzle with evaporimeter, evaporimeter top is provided with steam (vapor) outlet, described evaporimeter establishes the tubbiness of closed cavity to design in being, evaporator cavities internal fixtion is provided with ossiform taper deflector, described discharge nozzle penetrates evaporator cavities, discharge nozzle distal opening is just to taper deflector top, described taper deflector is provided with some fluid through-holes, described base of evaporator is also by being also communicated with the feed pipe between charging basket and feed pump by Matter Transfer pipe, base of evaporator is also provided with sample valve and concentrated solution drain valve.Described device can promote evaporation efficiency and solar energy utilization ratio to a great extent, decreases the consumption of other energy.
Description
Technical field
The utility model relates to solution concentration technique field, refers to a kind of solar energy evaporation concentration device especially.
Background technology
Usually can run in industrial production and daily life and carry out problem that is concentrated or recycling design to weak solution, most typical is exactly the utilization of evaporimeter and sea water purifier.What evaporimeter and sea water purifier all adopted is to weak solution heating, and solvent is volatilized with the object reaching concentrated solution or recycling design.Traditional approach utilizes fossil fuel or electric energy to heat weak solution.Along with the development in epoch, people faced by energy problem also more and more serious, therefore, the use of new forms of energy in solution evaporation and concentration field also more and more obtains the attention of people.Wherein the utilization of solar energy in this field is the most noticeable.
Solar energy evaporation concentration device is of a great variety on the market at present, but mostly has the shortcoming that evaporation efficiency is not high, heat energy utilization is insufficient.
Utility model content
The purpose of this utility model is: for the deficiencies in the prior art, and the utility model provides the high solar energy evaporation concentration device of a kind of evaporation efficiency.
For achieving the above object, the utility model is achieved through the following technical solutions: a kind of solar energy evaporation concentration device, comprise charging basket, solar energy heat collection pipe and evaporimeter, charging basket is communicated with by the feeding mouth of the feed pipe with solar energy heat collection pipe that are provided with feed pump, the discharging opening of solar energy heat collection pipe is communicated with evaporimeter by discharge nozzle, evaporimeter top is provided with steam (vapor) outlet, base of evaporator is provided with concentrated solution drain valve, it is characterized in that: described evaporimeter establishes the tubbiness of closed cavity to arrange in being, evaporator cavities internal fixtion is provided with taper deflector upwardly, described discharge nozzle penetrates evaporator cavities, discharge nozzle distal opening is just to taper deflector top, described taper deflector is provided with some fluid through-holes, described base of evaporator is also communicated with the feed pipe between charging basket and feed pump by Matter Transfer pipe, base of evaporator is also provided with sample valve.
By adopting such scheme, consequently: the use of taper deflector can make the material be heated launch as much as possible, expand disengagement area, taper deflector is provided with some fluid through-holes simultaneously, also can take away the steam of a part when high-temperature gas below taper deflector upwards flows, effectively improve the evaporation efficiency of described device.Simultaneously, base of evaporator is also provided with sample valve, can monitor the concentration of material in evaporimeter at any time, also be communicated with the feed pipe between charging basket and feed pump by Matter Transfer pipe when material concentration is not up to standard in evaporimeter, be heated further under the effect of feed pump, circulating and evaporating.
Of the present utility modelly to be set to further: outside described evaporimeter, bag is provided with insulation material.
By adopting such scheme, its effect is: effectively can prevent scattering and disappearing of heat energy, improve the utilization rate of solar thermal energy.
Of the present utility modelly to be set to further: be also provided with preheater between described charging basket and feed pump, described preheater is communicated with the steam (vapor) outlet on evaporimeter by high temperature steam pipe, and described high temperature steam pipe is provided with blower fan, is provided with distilled water outlet bottom preheater.
By adopting such scheme, its effect is: air pump can make pressure in evaporimeter reduce, and improves evaporation rate further, can also improve the enthalpy of steam, low temperature feed liquid, through preheater, can carry out heat exchange with high-temperature steam simultaneously, feed temperature raises, high-temperature steam cooling condensation.The program can obtain a large amount of high-purity solvent, can also improve the temperature of feed liquid, and the secondary strengthening heat energy utilizes, and improves the operating efficiency of said apparatus.
Of the present utility modelly to be set to further: the part on described feed pipe between preheater and feed pump is provided with inlet valve, described Matter Transfer pipe is positioned at and is provided with stop valve.
By adopting such scheme, its effect is: feed pump can extract low concentration feed liquid in charging basket and evaporimeter simultaneously, also optionally separately in charging basket or evaporimeter, extracts feed liquid.Different operations can be carried out according to actual conditions, reach production object.
In sum, a kind of solar energy solution condensing device provided by the utility model, can promote evaporation efficiency and solar thermal energy utilization rate to a great extent.Meanwhile, as far as possible few degree decreases the consumption of extra power, and therefore, a kind of solar energy solution condensing device provided by the utility model has good using value.
Accompanying drawing explanation
Fig. 1 is the utility model example structure schematic diagram,
Fig. 2 is the utility model embodiment taper deflector structure schematic diagram.
In figure: 1, charging basket, 2, solar energy heat collection pipe, 3, evaporimeter, 31, sample valve, 32, concentrated solution drain valve, 33, Matter Transfer pipe, 331, Matter Transfer valve, 34, high temperature steam pipe, 341, blower fan, 35, taper deflector, 351, fluid through-hole, 4, feed pipe, 41, inlet valve, 42, feed pump, 5, discharge nozzle, 6, preheater, 7, distilled water collector.
Detailed description of the invention
As depicted in figs. 1 and 2, this specific embodiment is a kind of solar energy solution condensing device.Comprise charging basket 1, solar energy heat collection pipe 2 and evaporimeter 3, charging basket 1 is communicated with by feed pipe 4 with the feeding mouth of solar energy heat collection pipe 2, feed pipe 4 is also provided with charging inlet valve 41 feed pump 42, the discharging opening of solar energy heat collection pipe 2 is communicated with by discharge nozzle 5 with evaporimeter 3, evaporimeter 3 top is provided with steam (vapor) outlet, the steam (vapor) outlet of evaporimeter 3 is communicated with preheater 6 by high temperature steam pipe 34, high temperature steam pipe 34 is provided with blower fan 341, and it is inner that the part helix on feed pipe 4 between charging basket 1 and inlet valve 41 is arranged on heat exchanger 6.Distilled water outlet bottom preheater 6 is communicated with condensate collector 7.Feed pump 42 is also communicated with bottom evaporimeter 3 by Matter Transfer pipe 33, and Matter Transfer pipe 33 is provided with stop valve 331, is provided with sample valve 31 and concentrated solution drain valve 32 bottom described evaporimeter 3.
Wherein, described evaporimeter 3 establishes the flexible of closed cavity in being, evaporimeter 3 cavity internal fixtion is provided with coniform deflector 351, described discharge nozzle 5 penetrates evaporimeter 3 cavity, discharge nozzle 5 distal opening is just to coniform deflector 35 top, and described coniform deflector 35 is provided with some fluid through-holes 351.
During work, material is extracted out by feed pump 42 from barrel 1, material is first through the preheating of preheater 6, then enter in solar energy heat collection pipe 2 and be heated, evaporimeter 3 is flowed into after material is heated, material launches evaporation on taper deflector 35, do not evaporate material and fall into base of evaporator through fluid through-hole 351, high-temperature steam is carried out preheating by blower fan 341 suction preheater 6 to material, steam condensation of catching a cold enters distilled water collector 7, in evaporimeter 3, material can sample through sample valve 31, when material concentration is below standard, solar energy heat collection pipe 2 can be reentered through Matter Transfer pipe 33 to be heated, circulation until in evaporimeter 3 material concentration up to standard, then material flows out through concentrated solution drain valve 32.
Claims (4)
1. a solar energy evaporation concentration device, comprise charging basket, solar energy heat collection pipe and evaporimeter, charging basket is communicated with by the feeding mouth of the feed pipe with solar energy heat collection pipe that are provided with feed pump, the discharging opening of solar energy heat collection pipe is communicated with evaporimeter by discharge nozzle, evaporimeter top is provided with steam (vapor) outlet, base of evaporator is provided with concentrated solution drain valve, it is characterized in that: described evaporimeter establishes the tubbiness of closed cavity to arrange in being, evaporator cavities internal fixtion is provided with taper deflector upwardly, described discharge nozzle penetrates evaporator cavities, discharge nozzle distal opening is just to taper deflector top, described taper deflector is provided with some fluid through-holes, described base of evaporator is also communicated with the feed pipe between charging basket and feed pump by Matter Transfer pipe, base of evaporator is also provided with sample valve.
2. a kind of solar energy evaporation concentration device according to claim 1, is characterized in that: outside described evaporimeter, bag is provided with insulation material.
3. a kind of solar energy evaporation concentration device according to claim 1 and 2, it is characterized in that: between described charging basket and feed pump, be also provided with preheater, described preheater is communicated with the steam (vapor) outlet on evaporimeter by high temperature steam pipe, described high temperature steam pipe is provided with blower fan, is provided with distilled water outlet bottom preheater.
4. a kind of solar energy evaporation concentration device according to claim 1 and 2, is characterized in that: the part on described feed pipe between preheater and feed pump is provided with inlet valve, described Matter Transfer pipe is positioned at and is provided with stop valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520056331.7U CN204543580U (en) | 2015-01-27 | 2015-01-27 | A kind of solar energy evaporation concentration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520056331.7U CN204543580U (en) | 2015-01-27 | 2015-01-27 | A kind of solar energy evaporation concentration device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204543580U true CN204543580U (en) | 2015-08-12 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520056331.7U Expired - Fee Related CN204543580U (en) | 2015-01-27 | 2015-01-27 | A kind of solar energy evaporation concentration device |
Country Status (1)
| Country | Link |
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| CN (1) | CN204543580U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105289038A (en) * | 2015-11-13 | 2016-02-03 | 浙江工贸职业技术学院 | Solar energy based apparatus for evaporating, separating, condensing and crystallizing solution |
-
2015
- 2015-01-27 CN CN201520056331.7U patent/CN204543580U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105289038A (en) * | 2015-11-13 | 2016-02-03 | 浙江工贸职业技术学院 | Solar energy based apparatus for evaporating, separating, condensing and crystallizing solution |
| CN105289038B (en) * | 2015-11-13 | 2017-03-29 | 浙江工贸职业技术学院 | A kind of solution evaporation based on solar energy separates concentration and crystallization apparatus |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150812 Termination date: 20200127 |