Hot-membrane co-production sea water desalination method
A seawater and thermal film technology, applied in chemical instruments and methods, seawater treatment, general water supply conservation, etc., can solve the problems of affecting the service life of permeable membranes, large membrane resistance, and high requirements for water temperature changes, reducing environmental thermal pollution, The effect of reducing the cost of fresh water and improving the mobility of the equipment
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0039] thermal production
[0040] ①The seawater pump 1 pumps seawater to the seawater cooling system 2 of the power plant, and the seawater passes through the seawater cooling system 2 of the power plant to reach a temperature of 24-35°C, and then the seawater is processed through the following route;
[0041] ②The first route, seawater enters the seawater desulfurization system 3 of the power plant, and the seawater desulfurization system 3 of the power plant is connected with the waste heat utilization system 4 of the flue gas of the power plant. 3;
[0042] ③ In the second route, seawater enters the flue gas waste heat utilization system 4 of the power plant, where the seawater and the flue gas at 140-150°C from the boiler of the power plant perform countercurrent heat exchange, and the flue gas temperature after heat exchange reaches 100-110°C. After the heat exchange, the seawater temperature reaches 60-80°C and enters the seawater desulfurization system 3, and the warm...
Embodiment 2
[0048] Membrane production
[0049] ①The seawater pump 1 pumps seawater to the seawater cooling system 2 of the power plant, and the seawater passes through the seawater cooling system 2 of the power plant and the temperature reaches 24-35°C;
[0050]② Membrane desalination system: Seawater enters seawater reverse osmosis device, seawater reverse osmosis device includes pretreatment device and desalination device; pretreatment device includes diversion micro-spin reaction tank 8, inclined plate sedimentation tank 9, V-shaped sand filter 10, clear water tank 11. R / O booster pump 12, high-efficiency filter 13 and safety filter 14; the desalination device includes a high-pressure feed water pump 15, an energy recovery device, a pressure boost system and a membrane desalination device 16.
[0051] The seawater enters the diversion micro-swirl reaction tank 8 for flocculation reaction, the reaction time is 20-30 minutes, the inlet flow velocity is 0.5-1m / s, gradually decreases, and...
Embodiment 3
[0063] Thermal film co-production
[0064] The seawater pump 1 pumps seawater to the seawater cooling system 2 of the power plant, and the seawater passes through the seawater cooling system 2 of the power plant to reach a temperature of 24-35°C, and then the seawater is processed through the following routes at the same time;
[0065] ②The first route, seawater enters the seawater desulfurization system 3 of the power plant, and the seawater desulfurization system 3 of the power plant is connected with the waste heat utilization system 4 of the flue gas of the power plant. 3;
[0066] ③ In the second route, seawater enters the flue gas waste heat utilization system 4 of the power plant, where the seawater and the flue gas at 140-150°C from the boiler of the power plant perform countercurrent heat exchange, and the flue gas temperature after heat exchange reaches 100-110°C. After the heat exchange, the seawater temperature reaches 60-80°C and enters the seawater desulfurizati...
PUM
| Property | Measurement | Unit |
|---|---|---|
| particle diameter | aaaaa | aaaaa |
| salt rejection rate | aaaaa | aaaaa |
| recovery rate | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 