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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

Active Publication Date: 2022-03-18
HUBEI TAISHENG CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The purpose of this technical invention is to propose a scheme for the utilization of ammonia water resources, which mainly solves the problems of the primary tail gas absorption tower, the The concentrated liquid from the tail gas absorption tower directly enters the dilute ammonia water together with the condensate ammonia water to transfer tanks, resulting in problems such as low concentration of dilute ammonia water (6% to 8%) and unstable concentration. The optimization process proposed by the present invention overcomes this technical difficulty , so that the concentration of ammonia water is stabilized in the range of 10%-15%, and it is produced into dilute ammonia water for export, so as to achieve the purpose of resource utilization

Method used

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  • A process and device for resource utilization of ammonia water
  • A process and device for resource utilization of ammonia water

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Experimental program
Comparison scheme
Effect test

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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Abstract

The process and device for resource utilization of ammonia water provided by the present invention, in order to ensure that the by-product ammonia water in the ammonia distillation section can be effectively resourced and utilized, aiming at the low and unstable ammonia concentration in the tail gas absorption tower in the original process, mainly through Change the circulation extraction mode of the absorption tower and replace the absorption liquid with soft water to improve the quality of ammonia water, replenish the concentrated liquid from the secondary absorption to the primary absorption tower as the absorption liquid, and replenish the concentrated liquid from the primary absorption tower to the ammonia distillation tower as the tower Top reflux, in order to optimize the ammonia distillation process. In the ammonia distillation system, only one side of the condensed ammonia water return tank is used to drain the concentration, which thoroughly and effectively controls the on-site odor caused by the irregular concentration of the two-stage tail gas absorption tower and the instability of the concentration of the two streams of ammonia water, and at the same time solves the concentration of ammonia water in the two-stage absorption liquid If the tower is too high, the packing tower will be blocked, and the pressure drop in the tower will increase, which will cause the liquid flooding in the tower, the tower will be flooded and other failure conditions, and overcome the problem that the concentration of ammonia water is too low to achieve resource recycling, so as to meet the use requirements of flue gas desulfurization and denitrification , to further reduce production costs.

Description

technical field [0001] The invention relates to a high-concentration ammonia nitrogen oxidation liquid stripping deammonization technology for recovering ammonia water, in particular to a process technology for resource utilization of ammonia water. Background technique [0002] Glyphosate crystallization liquid is a kind of wastewater produced in the process of producing glyphosate technical. Its composition is complex, mainly containing organic phosphorus, organic nitrogen and sodium chloride. Direct discharge will inevitably cause serious pollution to the environment. Our company currently The organic wastewater is treated by wet catalytic oxidation technology, the surface is yellow, the pH value is 8-9, and the ammonia nitrogen content of the oxidized wastewater is 4000-6000ppm. [0003] The ammonia nitrogen oxidation wastewater treatment process mentioned in the patent CN201720781613.2 uses a stripping deammonization tower to remove ammonia nitrogen. The tower top conde...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F9/10C01C1/02B01D53/18C02F101/16
CPCC02F9/00C01C1/022B01D53/18B01D53/1406C02F1/10C02F1/20C02F1/66C02F2101/16
Inventor 胡付超王瑞宝覃鹏辉王鹏胡波
Owner HUBEI TAISHENG CHEM