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Ammonia recycling method and system in APT production process

A production process and ammonia recovery technology, applied in the field of ammonia recovery technology, can solve the problems of uncompetitiveness of enterprises, increased cost, and low available value, etc., to improve stripping efficiency, save energy consumption, and improve ammonia activation efficiency Effect

Pending Publication Date: 2018-08-07
江西铜鼓有色冶金化工有限责任公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The specific idea is to make ammonium salt or ammonia water through the method of absorption. Although some methods solve the environmental protection problem, the usable value is not very high, and at the same time, additional costs will be added, making the enterprise uncompetitive.

Method used

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  • Ammonia recycling method and system in APT production process
  • Ammonia recycling method and system in APT production process
  • Ammonia recycling method and system in APT production process

Examples

Experimental program
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Effect test

Embodiment 1

[0052] Such as image 3 As shown, the ammonia recycling system of the present embodiment includes an evaporation pot 1, a centrifugal blower 2, a rectification tower 3, a heat exchanger 4, a stirring tank 5, a stripping tower 7 and a hydrochloric acid absorption tower 8, wherein the centrifugal blower 2 The inlet of the inlet is connected to the hot state ammonia outlet of the evaporator 1, the outlet is connected to the gas inlet 31 of the rectifying tower 3, the ammonia tail gas outlet 32 ​​of the rectifying tower 3 is connected to the inlet of the heat exchanger 4, and the outlet of the heat exchanger 4 is connected to the hydrochloric acid absorption tower The gas inlet 81 of 8; the outlet 33 at the bottom of the rectification tower 3 is connected to the inlet 51 of the stirring tank 5, and the waste water outlet 52 of the stirring tank 5 is connected to the liquid inlet 71 of the stripping tower 7 through the pump 6, and the waste gas outlet 53 is connected to the heat exc...

Embodiment 2

[0055] On the basis of Example 1, the device of the present invention is further described.

[0056] Such as image 3 As shown, the difference between the ammonia recycling system of this embodiment and that of Embodiment 1 is that the heat exchanger 4 is composed of a partitioned heat exchanger with high heat exchange efficiency; the stirring tank 5 adopts a mechanical stirring device with a large rotating speed, The solution is evenly dispersed, which can increase the activation rate of ammonia; the outlet 33 at the bottom of the rectification tower 3 and the position of the stripping tower 7 lower than the air outlet pipe 76 are equipped with ammonia nitrogen on-line monitors 34, 78, which accurately control the stillness after rectification. The residual liquid and the ammonia nitrogen content in the solution after stripping ensure that the ammonia nitrogen content of the waste water reaches the standard; the stripping tower 7 is also provided with a temperature controller...

Embodiment 3

[0059] On the basis of Example 2, the device of the present invention is further described.

[0060] Such as image 3 As shown, the ammonia recycling system of the present embodiment differs from Embodiment 2 in that there are four air outlet pipes 76 on the stripping tower 7, and the hydrochloric acid absorption tower 8 adopts corrosion-resistant, large gas-liquid contact area, In the sieve tray tower with high absorption efficiency, its spray device 83 includes two spray heads 831, 832 arranged horizontally and vertically, such as Figure 5 As shown, wherein the horizontal shower head 831 is an annular shower head, and the annular shower head is provided with a plurality of nozzles 833, and the vertical shower head 832 includes at least two parallel shower heads, and the parallel shower head is provided with a plurality of nozzles 833; The spray structure is coordinated to ensure that the gas phase and the liquid phase can fully contact, improve the absorption efficiency, a...

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Abstract

The invention provides an ammonia recycling method and a system in APT production process. The ammonia recycling method comprises following steps: 1, APT crystallization steam is discharged using a centrifugation blower fan, is introduced into a rectifying tower for rectification and condensation of ammonia tail gas to remove most water, and is introduced into a heat exchanger; 2, a three stage solution obtained via ion exchange is directly used for preparing a desorption agent, the rest ammonia nitrogen wastewater is pumped into a stirring tank, an alkali is added for ammonia activation, andgenerated ammonia tail gas is introduced into the heat exchanger; wastewater obtained via ammonia activation is pumped into an air stripping tower, and ammonia tail gas obtained via air stripping is introduced into the heat exchanger; when the ammonia-nitrogen value of obtained air stripping wastewater is detected to be qualified, discharging through a branch pipe is carried out, otherwise, the wastewater is pumped into the air stripping tower for air stripping; and 3, the temperature of the ammonia tail gas is reduced to be lower than 45 DEG C after treatment using the heat exchanger, the ammonia tail gas is introduced into a hydrochloric acid absorbing tower for circulating absorption, and an obtained solution is sent back to the main treatment stream directly for preparation of the desorption agent. The ammonia recycling method and the system are used for comprehensive treatment of ammonia nitrogen wastewater waste gas obtained in tungsten smelting, waste is changed into valuables,the method flow is simple, operation is convenient, the method is easy to control, and cost is low.

Description

technical field [0001] The invention relates to an ammonia recovery process, in particular to an ammonia recovery method and system in the APT production process. Background technique [0002] Due to the incomplete adsorption of ammonia-containing waste gas in the APT crystallization process, most of the ammonia-containing waste gas is difficult to recycle at present. The concentration of concentrated ammonia water recovered directly is low and has no use value, resulting in a large consumption of liquid ammonia and ammonium chloride. [0003] Ammonium paratungstate (APT) is produced through the ion exchange method of tungsten smelting. The ammonia nitrogen waste gas generated during the smelting process is mainly generated from the APT crystallization condensate water and part of the tail gas. The ammonia nitrogen waste water is mainly generated from the ion exchange and APT crystallization process in the APT production process. In the process of tungsten smelting, APT is p...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/00B01D53/78B01D53/58C02F9/10C02F101/16
CPCB01D53/005B01D53/58B01D53/78C02F1/02C02F1/20C02F1/66C02F2209/06C02F2101/16Y02A50/20
Inventor 刘恒嵩戴征文戴林明
Owner 江西铜鼓有色冶金化工有限责任公司
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