Seawater desalinization method and seawater desalinization device
A seawater and freshwater technology, used in seawater treatment, general water supply conservation, heating water/sewage treatment, etc., can solve the problems of unsatisfactory freshwater quality, low thermal energy recycling, and high manufacturing and maintenance costs, and is conducive to energy exchange and consumption. The effect of low power consumption and saving installation cost
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Example Embodiment
[0031] Example 1:
[0032] Reference figure 1 , The seawater desalination device of this embodiment includes a first jet circulation pump 2, a first condensation ejector 3, a first fresh water circulation tank 4 and a first evaporator 1. The lower part of the first fresh water circulation tank 4 is connected to the first evaporator 1 through a pipeline. The inlet end of the first evaporator 1 is connected to the inlet end of the first jet circulating pump 2 through a pipe, and the outlet end of the first jet circulating pump 2 is connected to the inlet end of the first condensation ejector 3 through a pipe, The outlet end of the first condensation ejector 3 is provided with a pipe whose nozzle extends into the first fresh water circulation tank 4, and the injection end interface of the first condensation ejector 3 is connected to the vacuum chamber of the first evaporator 1 through the pipe; A third heat exchanger is installed inside a fresh water circulation box 4; the outlet en...
Example Embodiment
[0040] Example 2:
[0041] The difference between the device of this embodiment and the device of embodiment 1 is that it also includes at least one recirculation evaporation concentration system, and the output end of the primary concentrated brine discharge pump 5 is connected to the recirculation evaporation concentration system.
[0042] This embodiment takes a recirculation evaporation and concentration system as an example for description.
[0043] Reference figure 2 The recirculation evaporative concentration system includes a fourth heat exchanger 18. The output end of the primary concentrated brine discharge pump 5 is connected to the inlet end of the fourth heat exchanger 18 through a pipe, and the outlet end of the fourth heat exchanger 18 passes through a pipe. Connected to the inlet end of the fifth heat exchanger placed in the second fresh water circulation tank 16, the outlet end of the fifth heat exchanger is connected to the second evaporator 13 through a pipe, and ...
Example Embodiment
[0051] Example 3:
[0052] The difference between the device of this embodiment and the device of embodiment 1 is that the first evaporator is replaced by a third evaporator 28 with a built-in condenser.
[0053] In this embodiment, a condenser is provided in the third evaporator 28. The inlet end of the condenser in the third evaporator 28 is the seawater inflow end, and the outlet end of the condenser in the third evaporator 28 passes through the pipe and the heater 30. The inlet end of the third evaporator 28 is connected to the condensate suction pump 24 below the condenser in the third evaporator 28, the outlet end of the heater 30 is connected to the third evaporator 28 through a pipe, and the third evaporator 28 is connected to the circulating pump through a pipe The inlet end of 20 is connected, the outlet end of the circulating pump 20 is connected to the inlet end of the third condensing ejector 21 through the pipe, and the outlet end of the third condensing ejector 21 is...
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