CN201779790U - Solar air pretreatment grading heat collection and liquor regenerating device - Google Patents
Solar air pretreatment grading heat collection and liquor regenerating device Download PDFInfo
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- CN201779790U CN201779790U CN2010202859290U CN201020285929U CN201779790U CN 201779790 U CN201779790 U CN 201779790U CN 2010202859290 U CN2010202859290 U CN 2010202859290U CN 201020285929 U CN201020285929 U CN 201020285929U CN 201779790 U CN201779790 U CN 201779790U
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Abstract
A solar air pretreatment grading heat collection and liquor regenerating device comprises an air circulating loop and a liquor circulating loop. The solar air pretreatment grading heat collection and liquor regenerating device has the advantages that 1 low-efficiency regeneration of a secondary heat collector/regenerator is compensated by high-efficiency regeneration of a primary heat collector/regenerator, 2 outdoor air is used for primary regeneration of low-concentration liquor, the low-concentration liquor after primary regeneration is then used for pre-humidifying outdoor air, and the pre-humidified dry air can realize effective regeneration of high-concentration liquor in the secondary heat collector/regenerator so that the heat accumulation capacity of the high-concentration liquor is improved, and 3 the solar air pretreatment grading heat collection/ liquor regenerating device has the outstanding advantages of sacrificing regenerated water evaporation rate of the low-concentration liquor on conditions of high temperature and low solar radiation, achieving the effect of improving water evaporation rate of the high-concentration liquor, and being especially suitable for Chinese southern areas with high-humidity weather.
Description
Technical field
The utility model relates to a kind of new type solar energy dehumidification solution regenerating unit, relates in particular to a kind of solar air pretreatment staged solution heat collection regeneration device.
Background technology
Breathe out in the conference of root weather at songbook, the Chinese government proposes the year two thousand twenty unit's GDP than decline 40%-45% in 2005, and energy-saving building technology will be the emphasis of following China science and technology research and development.Solar energy solution dehumidification Refrigeration Technique is regenerated owing to utilizing low-temperature heat sources such as solar energy, industrial waste heat to carry out solution, and possesses the accumulation of energy characteristic, will be the important technology that substitutes conventional compression formula refrigeration.Applying of it will greatly reduce the existing building energy consumption level, reduce carbon emission, alleviate the atmosphere greenhouse effects.
Solar energy is very suitable in the solution dehumidification Cooling Air-conditioning System solution being regenerated as a kind of regenerative resource of cleaning fully, moisturizes so that offset the solution dehumidification process, keeps the circular flow of dehumidification solution.In the process of utilizing solar energy that solution is regenerated, relate to two technical problems of solar energy heating and solution regeneration, Chinese scholars is with solar energy heating and the solution regeneration function structure solar energy heating/regenerator that is integrated in one, and this is a kind of efficient regenerative device of solution for experiment and theoretical validation.But China's south high humidity, low radiation weather can produce very big adverse effect to solar energy solution heat-collector/regenerability, because must remain on higher level in the temperature of this weather middle and high concentration solution regeneration, can reduce solar energy solution regeneration efficiency like this.Therefore, in high wetland, low surrounding areas, be necessary the direct thermal-arrest/regenerating unit of traditional solar energy solution is improved for guaranteeing solar energy solution regeneration efficiency.
Summary of the invention
The purpose of this utility model is to provide a kind of solar air pretreatment staged solution heat collection regeneration device, tradition sun solution heat-collector/regenerating unit increases with outdoor environment humidity and actified solution concentration, its regenerability (water evaporation rate) can greatly weaken, even the regeneration function failure phenomenon occurs.This method proposes a kind of under high humidity, low solar radiation weather, can realize highly concentrated solution is carried out effective regeneration.
The utility model is achieved like this, this device comprises air circulation loop and solution circulation loop, it is characterized in that air circulation loop is by blower fan, the air preprocessor, one-level thermal-arrest/regenerator, secondary thermal-arrest/regenerator, first air-valve, second air-valve is formed, air circulation loop is divided into one-level regeneration air loop and secondary regeneration air loop, wherein one-level regeneration air loop connected mode is as follows: the upper and lower side of one-level thermal-arrest/regenerator has air input a and air outlet slit end b, and the air outlet slit end b of one-level thermal-arrest/regenerator is connected with blower fan by the air airduct; Secondary regeneration air loop connected mode is as follows: the air outlet slit end d of air preprocessor is by air airduct and second air-valve air input f with the secondary thermal-arrest/regenerator that is connected in series after first air-valve is in parallel, and the air outlet slit end g of secondary thermal-arrest/regenerator is connected with blower fan by the air airduct; Solution circulation loop is by one-level thermal-arrest/regenerator, secondary thermal-arrest/regenerator, the air preprocessor, the one-level solution heat exchanger, the secondary solution heat exchanger, solution-water heat exchanger, the first listerine pump, the second listerine pump, the 3rd listerine pump, the 4th listerine pump is formed, solution circulation loop is divided into one-level actified solution loop, secondary actified solution loop and pre-dehumidification solution loop, one-level actified solution loop connected mode is as follows: the taphole end s of air preprocessor is connected with the solution arrival end k1 of one-level solution heat exchanger with the second listerine pump by one-level actified solution pipeline, the taphole end k2 of one-level solution heat exchanger is connected with the solution arrival end o of one-level thermal-arrest/regenerator, the taphole end r of one-level thermal-arrest/regenerator is connected with the solution arrival end k3 of one-level solution heat exchanger, and the taphole end k4 of one-level solution heat exchanger is connected with the solution arrival end t of air preprocessor with the first listerine pump by one-level actified solution pipeline; Secondary actified solution loop connected mode is as follows: the actified solution groove is connected with the solution arrival end h1 of secondary solution heat exchanger by secondary actified solution pipeline, the taphole end h2 of secondary solution heat exchanger is connected with the solution arrival end i of secondary thermal-arrest/regenerator by secondary actified solution pipeline, the taphole end q of secondary thermal-arrest/regenerator is connected with the solution arrival end h3 of secondary solution heat exchanger with the 3rd listerine pump by secondary actified solution pipeline, and the taphole end h4 of secondary solution heat exchanger connects the dehumidification solution groove by secondary actified solution pipeline; Pre-dehumidification solution loop connected mode is as follows: the taphole end u of air preprocessor is connected with the solution arrival end j1 of solution-water heat exchanger with the 4th listerine pump by pre-dehumidification solution pipeline, and the taphole end j2 of solution-water heat exchanger is connected with the air preprocessor by the solution output w of pre-dehumidification solution pipeline; The arrival end j3 of cooling water pipeline connects solution-water heat exchanger, and solution-water heat exchanger connects the port of export j4 of cooling water pipeline again.
Heat collector and regenerator are constituted one-level thermal-arrest/regenerator, secondary thermal-arrest/regenerator, and low concentration solution is at one-level thermal-arrest/regeneration in-situ regeneration, and highly concentrated solution is at secondary thermal-arrest/regeneration in-situ regeneration.
The one-level thermal-arrest/regenerator regeneration is directly taken from outdoor with air, the regeneration of the secondary thermal-arrest/regenerator mist of air from air preprocessor and surrounding air, low concentration solution the solution through one-level solution heat exchanger precooling after of solution that its preliminary treatment is required for coming out from one-level thermal-arrest/regenerator.
Aperture by changing first air-valve, second air-valve to be adapting to the variation of outdoor intensity of solar radiation and damp condition, when outdoor intensity of solar radiation is weak, turn down first air-valve during high humidity, open the aperture of big second air-valve to improve solution regeneration operating mode; Otherwise, drive big first air-valve, turn down the aperture of second air-valve.
Technique effect of the present utility model is: 1, I and II thermal-arrest/regenerator has been realized the fractional regeneration of low, high two kinds of concentration solution respectively, and inefficient regeneration compensates to secondary thermal-arrest/regenerator to utilize one-level thermal-arrest/regenerator high efficiency regeneration;
2, utilize outdoor air that low concentration solution is carried out one-level regeneration, with the low concentration solution after the one-level regeneration outdoor air is dehumidified in advance then, dry air after the pre-dehumidifying can be realized the effective regeneration of highly concentrated solution in secondary thermal-arrest/regenerator, has improved the accumulation of energy ability of highly concentrated solution;
3, the outstanding advantage of solar air pretreatment staged solution heat collection/regenerating unit of the present utility model is the water evaporation rate of sacrificing low concentration solution regeneration under high humidity, low solar radiation condition, reach the effect that improves the highly concentrated solution water evaporation rate, be particularly suitable for high humidity weather area, China south.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
One-level thermal-arrest/regenerator 2, secondary thermal-arrest/regenerator 3, air preprocessor 4, one-level solution heat exchanger 5, secondary solution heat exchanger 6, blower fan 7, the first listerine pump 8, the second listerine pump 9, the 3rd listerine pump 10, the 4th listerine pump 11, solution-water heat exchanger 12, first air-valve 13, second air-valve 14, air airduct 15, one-level actified solution pipeline 16, secondary actified solution pipeline 17, pre-dehumidification solution pipeline 18, cooling water pipeline 19, dehumidification solution groove 20, actified solution groove in the drawings, 1,
The specific embodiment
As shown in Figure 1, the technical solution of the utility model is further described, and solar air pretreatment staged solution heat collection/regenerating unit of the present utility model comprises air circulation loop and solution circulation loop; Air circulation loop is made up of blower fan 6, air preprocessor 3, one-level thermal-arrest/regenerator 1, secondary thermal-arrest/regenerator 2, first air-valve 12, second air-valve 13, and its flow process is divided into one-level regeneration air loop and secondary regeneration air loop.One-level regeneration air loop connected mode is as follows: outdoor air enters one-level thermal-arrest/regenerator 1 by the first air input a, the air outlet slit end b of one-level thermal-arrest/regenerator 1 is connected with blower fan 6 by airduct 14, and blower fan 6 is discharged to environment from the air output end p with air.Secondary regeneration air loop connected mode is as follows: outdoor air enters system from air input c and air input e respectively, enter the air intake end f of secondary thermal-arrest/regenerator 2 after wherein the air outlet slit end d of air preprocessor 3 converges with the surrounding air of coming from first air-valve 12 by the airduct 14 and second air-valve 13, the air outlet slit end g of secondary thermal-arrest/regenerator 2 is connected with blower fan 6 by airduct 14; Solution circulation loop is by one-level thermal-arrest/regenerator 1, secondary thermal-arrest/regenerator 2, air preprocessor 3, one-level solution heat exchanger 4, secondary solution heat exchanger 5, solution-water heat exchanger 11, the first listerine pump 7; The second listerine pump 8; The 3rd listerine pump 9; The 4th listerine pump 10 is formed, and its flow process is divided into one-level actified solution loop, secondary actified solution loop and pre-dehumidification solution loop.One-level actified solution loop connected mode is as follows: the taphole end s of air preprocessor 3 is connected with the solution arrival end k1 of one-level solution heat exchanger 4 with the second listerine pump 8 by one-level actified solution pipeline 15, the taphole end k2 of one-level solution heat exchanger 4 is connected with the solution arrival end o of one-level thermal-arrest/regenerator 1, the taphole end r of one-level thermal-arrest/regenerator 1 is connected with the solution arrival end k3 of one-level solution heat exchanger 4, and the taphole end k4 of one-level solution heat exchanger 4 is connected with the solution arrival end t of air preprocessor 3 with the first listerine pump 7 by one-level actified solution pipeline 15.Secondary actified solution loop connected mode is as follows: actified solution groove 20 is connected with the solution arrival end h1 of secondary solution heat exchanger 5 by secondary actified solution pipeline 16, the taphole end h2 of secondary solution heat exchanger 5 is connected with the solution arrival end i of secondary thermal-arrest/regenerator 2 by secondary actified solution pipeline 16, the taphole end q of secondary thermal-arrest/regenerator 2 is connected with the solution arrival end h3 of secondary solution heat exchanger 5 with the 3rd listerine pump 9 by secondary actified solution pipeline 16, and the taphole end h4 of secondary solution heat exchanger 5 enters dehumidification solution groove 19 by secondary actified solution pipeline 16.Pre-dehumidification solution loop connected mode is as follows: the taphole end u of air preprocessor 3 is connected with the solution arrival end j1 of solution-water heat exchanger 11 with the 4th listerine pump 10 by pre-dehumidification solution pipeline 17, and the taphole end j2 of solution-water heat exchanger 11 is connected with air preprocessor 3 by the solution output w of pre-dehumidification solution pipeline 17; In addition, cooling water enters solution-water heat exchanger 11 by cooling water inlet end j3, after supercooled water port of export j4 leaves system.
Outdoor air directly enters one-level thermal-arrest/regenerator 1 and low concentration solution (interior circulation solution) wherein carries out heat and mass, absorbs in the weak solution to be discharged to outdoor environment behind the moisture, constitutes one-level regeneration air loop.The secondary regeneration air is respectively from air preprocessor 3 and outdoor environment, enter after both mix secondary thermal-arrest/regenerator 2 absorb wherein be discharged to behind interior the moisture of highly concentrated solution (purpose solution) outdoor, formation secondary regeneration air loop.One-level actified solution loop is circulation in a kind of device, and the low concentration solution of its circulation flows among one-level thermal-arrest/regenerator 1, air preprocessor 3, one-level solution heat exchanger 4 and one-level actified solution pipeline 15 repeatedly.Secondary actified solution loop is an extension tube attached loop, the highly concentrated solution of the need regeneration of coming out from external regeneration solution tank 20 enters secondary thermal-arrest/regenerator 2 behind secondary solution heat exchanger 5 pre-heating temperature elevations earlier, via 5 precoolings of secondary solution heat exchanger, get back in the outside dehumidification solution groove 19 afterwards.Pre-dehumidification solution loop also is circulation in a kind of device, it is in air preprocessor 3 inner loop, 10 pressurizations enter 11 coolings of solution-water heat exchanger to the pre-dehumidification solution that comes out from the bottom reservoir of air preprocessor 3 through the 4th listerine pump, flow into afterwards in the cloth liquid bath on preprocessor top, in the cloth liquid bath solution by self gravitation descending flow with wherein in advance dehumidified air contact, absorb moisture in the pre-dehumidified air.Heat collector and regenerator are constituted one-level thermal-arrest/regenerator 1, secondary thermal-arrest/regenerator 2, and low concentration solution is regenerated in one-level thermal-arrest/regenerator 1, and highly concentrated solution is regenerated in secondary thermal-arrest/regenerator 2.1 regeneration of one-level thermal-arrest/regenerator is directly taken from outdoor with air, the regeneration of secondary thermal-arrest/regenerator 2 mist of air from air preprocessor 3 and surrounding air, low concentration solution the solution through one-level solution heat exchanger 4 precoolings after of solution that its preliminary treatment is required for coming out from one-level thermal-arrest/regenerator 1.Aperture by changing first air-valve 12, second air-valve 13 to be adapting to the variation of outdoor intensity of solar radiation and damp condition, when outdoor intensity of solar radiation is weak, turn down first air-valve 12 during high humidity, open the aperture of big second air-valve 13 to improve solution regeneration operating mode; Otherwise, drive big first air-valve 12, turn down the aperture of second air-valve 13.
Claims (1)
1. solar air pretreatment staged solution heat collection regeneration device, this device comprises air circulation loop and solution circulation loop, it is characterized in that air circulation loop is by blower fan, the air preprocessor, one-level thermal-arrest/regenerator, secondary thermal-arrest/regenerator, first air-valve, second air-valve is formed, air circulation loop is divided into one-level regeneration air loop and secondary regeneration air loop, wherein one-level regeneration air loop connected mode is as follows: the upper and lower side of one-level thermal-arrest/regenerator has air input a and air outlet slit end b, and the air outlet slit end b of one-level thermal-arrest/regenerator is connected with blower fan by the air airduct; Secondary regeneration air loop connected mode is as follows: the air outlet slit end d of air preprocessor is by air airduct and second air-valve air input f with the secondary thermal-arrest/regenerator that is connected in series after first air-valve is in parallel, and the air outlet slit end g of secondary thermal-arrest/regenerator is connected with blower fan by the air airduct; Solution circulation loop is by one-level thermal-arrest/regenerator, secondary thermal-arrest/regenerator, the air preprocessor, the one-level solution heat exchanger, the secondary solution heat exchanger, solution-water heat exchanger, the first listerine pump, the second listerine pump, the 3rd listerine pump, the 4th listerine pump is formed, solution circulation loop is divided into one-level actified solution loop, secondary actified solution loop and pre-dehumidification solution loop, one-level actified solution loop connected mode is as follows: the taphole end s of air preprocessor is connected with the solution arrival end k1 of one-level solution heat exchanger with the second listerine pump by one-level actified solution pipeline, the taphole end k2 of one-level solution heat exchanger is connected with the solution arrival end o of one-level thermal-arrest/regenerator, the taphole end r of one-level thermal-arrest/regenerator is connected with the solution arrival end k3 of one-level solution heat exchanger, and the taphole end k4 of one-level solution heat exchanger is connected with the solution arrival end t of air preprocessor with the first listerine pump by one-level actified solution pipeline; Secondary actified solution loop connected mode is as follows: the actified solution groove is connected with the solution arrival end h1 of secondary solution heat exchanger by secondary actified solution pipeline, the taphole end h2 of secondary solution heat exchanger is connected with the solution arrival end i of secondary thermal-arrest/regenerator by secondary actified solution pipeline, the taphole end q of secondary thermal-arrest/regenerator is connected with the solution arrival end h3 of secondary solution heat exchanger with the 3rd listerine pump by secondary actified solution pipeline, and the taphole end h4 of secondary solution heat exchanger connects the dehumidification solution groove by secondary actified solution pipeline; Pre-dehumidification solution loop connected mode is as follows: the taphole end u of air preprocessor is connected with the solution arrival end j1 of solution-water heat exchanger with the 4th listerine pump by pre-dehumidification solution pipeline, and the taphole end j2 of solution-water heat exchanger is connected with the air preprocessor by the solution output w of pre-dehumidification solution pipeline; The arrival end j3 of cooling water pipeline connects solution-water heat exchanger, and solution-water heat exchanger connects the port of export j4 of cooling water pipeline again.
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| Application Number | Priority Date | Filing Date | Title |
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| CN2010202859290U CN201779790U (en) | 2010-08-09 | 2010-08-09 | Solar air pretreatment grading heat collection and liquor regenerating device |
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| CN2010202859290U CN201779790U (en) | 2010-08-09 | 2010-08-09 | Solar air pretreatment grading heat collection and liquor regenerating device |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN101900389A (en) * | 2010-08-09 | 2010-12-01 | 南昌大学 | Solar air pretreatment staged solution heat collection regeneration device |
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| CN101900389A (en) * | 2010-08-09 | 2010-12-01 | 南昌大学 | Solar air pretreatment staged solution heat collection regeneration device |
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Granted publication date: 20110330 Termination date: 20120809 |