Unlock instant, AI-driven research and patent intelligence for your innovation.

Ammonia water resource utilization process and device

A technology of resource utilization and ammonia water, applied in the fields of ammonia compounds, inorganic chemistry, water pollutants, etc., can solve the problems of low concentration and unstable concentration of dilute ammonia water, and achieve cost savings, obvious environmental protection benefits, and unstable concentration control. Effect

Active Publication Date: 2020-07-10
HUBEI TAISHENG CHEM
View PDF8 Cites 3 Cited by
  • 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

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Ammonia water resource utilization process and device
  • Ammonia water resource utilization process and device

Examples

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...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention provides an ammonia water resource utilization process and device. In order to ensure that the byproduct ammonia water in the ammonia distillation section can be effectively recycled, the ammonia water quality is improved by mainly changing the cyclic recovery mode of an absorption tower and replacing absorption liquid with soft water by aiming at the conditions of low ammonia concentration and instability of a tail gas absorption tower in the original process, concentrated liquor discharged by secondary absorption is supplemented to a primary absorption tower to serve as absorption liquid, and concentrated liquor discharged by the primary absorption tower is supplemented to an ammonia distillation tower to serve as tower top reflux so that the ammonia distillation technological process is optimized. Only one part of the condensed ammonia water reflux tank of the ammonia distillation system discharges concentrated ammonia water, and the problems of field peculiar smell and unstable concentration of two strands of ammonia water caused by irregular concentration discharge of the two-stage tail gas absorption tower are thoroughly and effectively controlled; meanwhile, the fault working conditions of flooding, flooding and the like in the tower caused by blockage of the packed tower and increase of tower pressure drop due to over-high ammonia water concentration in the two-stage absorption liquid are solved, and the problem that resource recycling cannot be realized due to over-low ammonia water concentration is solved and thus the use requirement of flue gas desulfurization and denitrification is met and the production cost is further reduced.

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

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Applications(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