The air-conditioning system of air source heat pump solid absorption dehumidifying
Technical field
Patent of the present invention relates to the air-conditioning system of a kind of solid absorption dehumidifying, belongs to building energy saving field.
Background technology
The air-conditioning system of the solid absorption dehumidifying of development in recent years, owing to not needing low-temperature heat source to dehumidify, not only energy-conservation but also be conducive to health, using air source heat pump as this technology of the cold and heat source of this system, develop to some extent, but, due to the necessary pair-wise combination of solid adsorption dehumidification device, after its adsorption and dehumidification, regenerative process is also wanted to run continuously, therefore, two cover air source heat pump lists be adopted for dehumidifying service, then uneconomical.How to make two cover heat pumps used both bear room cooling, can bear dehumidifying again, and can realize independent temperature-humidity control, be the problem needing to solve.
Summary of the invention
The present invention, in order to overcome above-mentioned air source heat pump solid absorption dehumidifier shortcoming, proposes following technical scheme: namely by the fin tube bundle A of the bonding silica gel of a pair parallel connection, B, replaces the condenser in an air source heat pump, retains its remaining part, i.e. compressor C, the indoor fluorine of capillary 1 and the evaporimeter as heat pump heat distribution system---air heat exchanger 3, so the heating forming air source heat pump, can realize the heating of silica gel, regeneration, then by the fin tube bundle A of the bonding silica gel of described parallel connection, B, replaces the evaporimeter in another air source heat pump, retains its remaining part, i.e. compressor D, capillary 2 and the outdoor fluorine as its condenser---air heat exchanger 4, form air source heat pump refrigeration system, can realize the cooling of silica gel, described heat pump heats, in refrigeration system, with A in parallel, the inlet tube that B is connected has import threeway 17, 18, outlet has outlet threeway 19, 20, conflux arm and the shunt pipe of each threeway is equipped with magnetic valve, namely magnetic valve 9 is housed on 17, 10, be equipped with 11 on 18, 12, be equipped with 13 on 19, 14, be equipped with 15 on 20, 16, amount to eight.
Eight described magnetic valves, are divided into two groups, periodically open in turn, namely 9,10,11,12 open simultaneously, coordinate compressor C to open, silica gel A regeneration regime can be obtained, after a period of time, 13,14,15,16 open simultaneously, coordinate compressor D to open, silica gel cooling absorption working condition can be obtained.
Described indoor fluorine---air heat exchanger 3 is mounted in air-conditioned room, compressor C suction temperature, pressure can be made higher, thus outlet obtain high temperature, high pressure, meets silica regeneration requirement, meanwhile, indoor fluorine---air heat exchanger 3 is to air-conditioned room cooling.
Solid absorption dehumidifier/air-conditioning system of the present invention is formed by above-mentioned silica gel heating regenerative system and cooling adsorption system summation.
Accompanying drawing explanation
Fig. 1 is the air-conditioning system schematic diagram of solid absorption dehumidifying.
In figure: A, B---the fin tube bundle of a pair bonding silica gel; C, D---compressor; 1,2---capillary; 3---indoor fluorine---air heat exchanger; 4---outdoor fluorine---air heat exchanger; 5---high steam pressing tube; 6---high-pressure liquid tube; 7---low hydraulic fluid pipe; 8---low pressure steam pipe; 9,10---magnetic valve; 11,12---magnetic valve; 13,14---magnetic valve; 15,16---magnetic valve; 17---fin tube bundle A import threeway; 18---fin tube bundle B import threeway; 19---fin tube bundle A exports threeway; 20---fin tube bundle B exports threeway.
Detailed description of the invention
As shown in Figure 1, open compressor C and D, magnetic valve 9,11,14,16, the high pressure vapour of compressor C is along high steam pressing tube 5, through magnetic valve 9, fin tube bundle A import threeway 17, after passing into the fin tube bundle A heat release of bonding silica gel, threeway 19 is exported through fin tube bundle A, through magnetic valve 11, high-pressure liquid tube 6, low hydraulic fluid is become, through low hydraulic fluid pipe 7, by indoor fluorine by capillary 1---air heat exchanger 3, absorb Indoor Thermal, refrigeration, after become low-pressure steam and return compressor C through low pressure steam pipe 8, the silica gel on fin tube bundle A is regenerated;
Simultaneously, the high pressure vapour of compressor D is through high steam pressing tube 5, outdoor fluorine---air heat exchanger 4, high pressure liquid is become after outdoor heat release, become low hydraulic fluid through high-pressure liquid tube 6, capillary 2, through low hydraulic fluid pipe 7, magnetic valve 14, fin tube bundle B import threeway 18, enter the fin tube bundle B of bonding silica gel, threeway 20, magnetic valve 16 is exported by fin tube bundle B by after silica gel cooling, return compressor through low pressure steam pipe 8, fin tube bundle B is cooled, there is adsorption capacity;
After a certain time period, magnetic valve 10,12,13,15 is opened, the high pressure vapour of compressor C is along high steam pressing tube 5, through magnetic valve 10, fin tube bundle B import threeway 18, pass into the fin tube bundle B of bonding silica gel, threeway 20, magnetic valve 12 is exported by high-pressure liquid tube 6 through fin tube bundle B after heat release, low hydraulic fluid is become by capillary 1, through low hydraulic fluid pipe 7, through indoor fluorine---air heat exchanger 3, absorb Indoor Thermal, the low-pressure steam after refrigeration returns compressor C along low pressure steam pipe 8, and the silica gel on fin tube bundle B is regenerated;
Meanwhile, the high pressure vapour of compressor D is through high steam pressing tube 5, through outdoor fluorine---air heat exchanger 4, high pressure liquid is become after outdoor heat release, through high-pressure liquid tube 6, low hydraulic fluid is become through capillary 2, through low hydraulic fluid pipe 7, magnetic valve 13, fin tube bundle A import threeway 17 enters the fin tube bundle A of bonding silica gel, by the silica gel cooling after regeneration, low-pressure steam is become after making that there is adsorption capacity, threeway 19 is exported through fin tube bundle A, again through magnetic valve 15, compressor D is returned along low pressure steam pipe 8, so complete the regeneration in turn of a pair silica gel on fin tube bundle and cool in turn, and there is a process of adsorption capacity, silica gel in the process can moisture in continuous adsorption air, accomplish continuous dehumidifying.
Said process can carry out continuously on demand.