A process and device for resource utilization of ammonia water
A technology of resource utilization and ammonia water, which is applied in the direction of ammonia compounds, inorganic chemistry, water pollutants, etc., can solve the problems of low concentration and unstable concentration of dilute ammonia water, and achieve the goal of saving treatment costs, obvious environmental protection benefits, and controlling unstable concentration Effect
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Embodiment 1
[0037] An ammonia water resource utilization device, the outlet of the oxidizing liquid feeding pump 2 is connected to the material inlet of the oxidizing liquid feeding plate heat exchanger 3 through a pipeline; the material outlet of the oxidizing liquid feeding plate heat exchanger 3 is connected to the stripping deamination tower through a pipeline 4. The inlet is connected; the gas phase outlet of the stripping deamination tower 4 is connected to the gas phase inlet of the ammonia condenser 5 through a pipeline, the liquid phase outlet of the ammonia condenser 5 is connected to the inlet of the condensed ammonia water return tank 6, and the liquid phase outlet 6 of the condensed ammonia water return tank is passed through The condensed ammonia water reflux / production pump 7 is connected to the ammonia water delivery pipeline and the inlet of the transfer tank 15 in dilute ammonia water and the return pipeline of the stripping deamination tower 4, and the outlet of the trans...
Embodiment 2
[0043] After adjusting the pH value of the oxidizing solution to 8.5, the oxidizing solution feed pump is fed at a rate of 50m 3 The flow rate of / h enters the system, heats up to 80°C after heat exchange with the oxidizing liquid feed plate heat exchanger, and then enters the stripping deamination tower. distilled from the top. The stripping deamination tower is a sieve-plate atmospheric stripping tower, and the feeding method is from the bottom of the tower. In addition, a reboiler is installed at the bottom of the tower to raise the temperature by steam. The steam pressure is 0.5Mpa, the temperature at the bottom of the tower is 90°C, and the temperature at the top of the tower 80°C; while maintaining a certain liquid level at the bottom of the tower, the deammonization and oxidation liquid is continuously extracted through the deammonization and oxidation liquid extraction circulation pump, and the liquid level of the deammonization tower is stripped from the deammonizatio...
Embodiment 3
[0048] After adjusting the pH value of the oxidizing solution to 8.2, the oxidizing solution feed pump is fed at a rate of 50m 3 The flow rate of / h enters the system, heats up to 80°C after heat exchange with the oxidizing liquid feed plate heat exchanger, and then enters the stripping deamination tower. distilled from the top. The stripping deamination tower is a sieve-plate atmospheric stripping tower, and the feeding method is the bottom of the tower, and a reboiler is installed at the bottom of the tower, and the temperature is raised by steam. The steam pressure is 0.5Mpa, the bottom temperature is 85°C, and the top temperature is 75°C; while maintaining a certain liquid level at the bottom of the tower, the deammonization and oxidation liquid is continuously extracted through the deammonization and oxidation liquid extraction circulation pump, and the liquid level of the deammonization tower is stripped with the deammonization and oxidation liquid extraction circulation...
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