Efficient solar seawater desalination and air conditioner refrigeration combined operation method and system thereof
An air-conditioning refrigeration and operation system technology, which is applied to chemical instruments and methods, refrigerators, seawater treatment, etc., can solve the problems of high renovation requirements, reduced service life of air-conditioning systems, and inability to desalinize seawater, so as to save cooling water and utilize High efficiency, beneficial to the effect of environmental protection
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Embodiment 1
[0036] Such as figure 1 As shown, the high-efficiency solar desalination and air-conditioning refrigeration combined operation system designed by the present invention includes solar heat collection system I, seawater desalination system II and absorption air conditioning system III. Among them: the main part of the solar heat collection system I is the solar heat collector 17, which adopts a medium-high temperature heat collector. Such as figure 2 As shown, the solar heat collector 17 is provided with a heat transfer working medium input port 17.1 of the heat collection system, a heat transfer working medium output port 17.2 of the heat collection system, and a heat transfer working medium circulation pump 18 . The seawater desalination system II includes a distillation system 27 and a heat exchange system 28 .
[0037] Such as figure 1 , Figure 7 As shown, the distillation system 27 includes three distillers, which are respectively the primary distiller 16, the seconda...
Embodiment 2
[0046] In this embodiment, the overall structure is similar to Embodiment 1, the difference is:
[0047] Such as Figure 5 As shown, the distillation system 27 only includes the first-stage still 16, the seawater input port 27.1 of the distillation system, the brine output port 27.2 of the distillation system, the steam output port 27.3 of the distillation system, the heat transfer medium input port 27.4 of the distillation system, the heat transfer port of the distillation system The mass output ports 27.5 are all arranged on the primary still 16. Part of the steam generated by the primary still 16 heated by the heat transfer medium is input into the absorption air conditioning system III as a heat source, and the other part is input into the steam condensing device 29 for condensation.
[0048] Such as image 3 As shown, the absorption air conditioning system III is a single-effect lithium bromide air conditioner, which is different from the double-effect lithium bromide a...
Embodiment 3
[0050] In this embodiment, the overall structure is similar to Embodiment 1, the difference is:
[0051] Such as Figure 6 As shown, the distillation system 27 is composed of a primary distiller 16 and a secondary distiller 15. The seawater input port 27.1 of the distillation system and the heat transfer working medium input port 27.4 of the distillation system are arranged on the primary distiller 16. The brine output port of the distillation system is 27.2. The heat transfer working medium outlet 27.5 of the distillation system is set on the secondary distiller 15 . The steam output port 27.3 of the distillation system includes an air-conditioning steam output port 27.3a provided on the primary distiller 16, and an evaporation steam output port 27.3c provided on the secondary distiller 15. The seawater output port of the primary distiller 16 is connected with the seawater input port of the secondary distiller 15 , and the heat transfer working medium output port of the prim...
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