Super-gravity concentration difference power generation device and method
A power generation device and super-gravity technology, which is applied in the direction of machines/engines, mechanisms for generating mechanical power, mechanical equipment, etc., can solve the problems of high-efficiency energy recovery devices such as high prices, unfavorable cycle ratios, and reduced technical and economic value of the system to achieve high Technical and economic value, simple system structure, automatic and efficient recovery effect
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Embodiment 1
[0020] Embodiment 1, figure 1 Provided is a supergravity concentration difference power generation device and method. The supergravity concentration power generation device includes a power generation device and a pressure concentration difference work device; the power generation device is a liquid turbine 3 , and the pressure concentration difference work device is a permeator 4 .
[0021] The inlet side of the liquid turbine 3 is provided with a pure water inlet 6, and there is a pipe I connection between the inlet of the liquid turbine 3 and the pure water inlet 6. The pure water inlet 6 is connected to a pure water storage tank and other devices, and through the pure water storage tank The pure water is drawn out by other devices and imported into the liquid turbine 3; the outlet of the liquid turbine 3 is connected to the liquid inlet I of the permeator 4, and the pure water in the liquid turbine 3 is introduced into the permeator 4 through the liquid inlet; the solution...
Embodiment 1
[0032] The calculation parameters of implementation example 1 are shown in Table 1 (for 1 kg of water). The design conditions are: the radius of gyration of the system is 0.5m, the chemical energy contained in the calcium chloride solution and pure water is used for concentration difference power generation, the concentration of the concentrated calcium chloride solution is 18%, the temperature is 25°C, and the osmotic pressure is 11Mpa. When the cycle rate is 4 times (defined as the ratio of dilute solution to water), the concentration of the dilute solution obtained is 13.5%, the osmotic pressure is 8.3Mpa, the average driving pressure difference of the pressure-delayed osmotic process is 3.1Mpa, and the system speed is 2045 rpm / min, solution pump efficiency is 80%, power consumption is 0.67kJ / kg, liquid turbine efficiency is 80%, output work is 4.34kJ / kg, system net output work is 3.67kJ / kg, system exergy efficiency (defined as The ratio of the theoretical work to the net ...
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