Gas-phase rectifying method for steam containing ammonia in APT (ammonium paratungstate) production process and equipment

A production process and ammonia steam technology, applied in the field of gas phase distillation of ammonia-containing steam, can solve the problems of low concentration of recycled ammonia water and low recovery rate of ammonia gas, and achieve the goal of satisfying the balance of ammonia water, reducing the treatment capacity and increasing the concentration of ammonia water Effect

Active Publication Date: 2013-09-11
NANJING GW ENVIRONMENT ENG
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0010] The present invention aims at the problem of ammonia-containing steam treatment in the existing APT production process, low ammonia gas recovery rate, and low concentration of recycled ammonia water, and invents a g

Method used

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  • Gas-phase rectifying method for steam containing ammonia in APT (ammonium paratungstate) production process and equipment

Examples

Experimental program
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Effect test

Embodiment 1

[0032] as attached figure 1 The vapor phase rectification technology of ammonia-containing steam in the shown a kind of APT production process, its step is:

[0033] (1) Ammonia gas absorption cycle: the ammonia-containing steam at 102-107°C from the evaporation and crystallization unit enters the top condenser 2 of the vapor phase rectification tower, and the ammonia-containing vapor is condensed into dilute Ammonia water, dilute ammonia water enters tower top reflux tank 3, meanwhile, the high-concentration ammonia gas that extracts from tower top condenser 2 enters ammonia gas absorption tower 5, and the bottom of ammonia gas absorption tower 5 is provided with absorption liquid, is driven into concentrated ammonia water by pump Condenser 6, after the absorption liquid is condensed, it enters the top of the ammonia gas absorption tower 5, sprays from top to bottom, contacts with the high-concentration ammonia gas produced by the top condenser 2, and the absorption liquid at...

Embodiment 2

[0038] The difference between Example 2 and Example 1 is that in step (1) of Example 2, the ammonia-containing steam passes through the heat exchanger 1 between the tower top condenser, and after the ammonia-containing steam is initially cooled by the heat exchanger, the ammonia-containing steam contains The temperature of the ammonia vapor drops to 60-70°C, and then enters the top condenser 2 for secondary condensation, and the temperature drops to 30-40°C; the low-concentration deammonification wastewater at the bottom of the vapor phase distillation tower 4 also enters the heat exchanger 1 , to lower the temperature of the ammonia-containing steam; in addition, in step (2), the liquid caustic soda added at the bottom of the gas-phase rectification tower 4 is 30% NaOH, and the pH of dilute ammonia water at the bottom of the tower is adjusted to be >14; When the concentration of ammonia nitrogen in the deamination wastewater is less than 100 mg / L, it is sent to the nitrogen st...

Embodiment 3

[0040] A kind of equipment for the gas phase rectification method of embodiment 1 or embodiment 2, it is characterized in that each part and connection relation are: the steam pipeline containing ammonia is connected with the tower top condenser 2 inlet of gas phase rectification tower, and described tower The top condenser 2 top outlet is connected with the ammonia absorption tower 5 inlets, and the bottom of the ammonia absorption tower 5 is connected with the bottom end of the strong ammonia water condenser 6 and the ammonia water tank 10 through a pump, and the top of the strong ammonia water condenser 6 is connected with the ammonia water tank 10. The middle part of the gas absorption tower 5 is connected; the bottom outlet of the tower top condenser 2 is connected to the top of the gas phase rectification tower 4 through the tower top reflux tank 3, and the bottom of the gas phase rectification tower 4 is connected with an alkali injection device and steam Injection devic...

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Abstract

The invention discloses a gas-phase rectifying method for steam containing ammonia in the APT (ammonium paratungstate) production process, which is characterized by comprising the following steps of: primary cooling of steam containing ammonia, direct entry of the steam containing ammonia into a condenser on the top of a rectifying tower, gas-phase steamed ammonia cycle of low-concentration ammonia at the bottom of the rectifying tower, and ammonia absorption cycle of an ammonia absorption tower. The invention further provides a set of equipment used for the gas-phase rectifying method. The problems of the difficulty of steam containing ammonia recovery and tail gas treatment in the existing APT production process are solved, and the problems that the concentration of the recovered ammonia is low and the water balance for ammonia reuse of the whole factory cannot be realized are solved by using the gas-phase rectifying method. The gas-phase rectifying method for the steam containing ammonia in the APT production process is invented to increase the concentration of the recovered ammonia and realize the water balance for ammonia reuse of the whole factory, so that all water containing ammonia of the whole factory can be reused, and the ammonia recovery ratio in the APT production process is greatly increased.

Description

technical field [0001] The invention relates to a gas-phase rectification technology for ammonia-containing steam, in particular to a gas-phase rectification method and equipment for ammonia-containing steam in the APT production process. Background technique [0002] In the process of producing ammonium paratungstate (APT) by wet smelting of tungsten, the sodium tungstate solution is transformed into ammonium tungstate solution through extraction, and the ammonium tungstate solution is evaporated and concentrated into ammonium paratungstate product. The production of 1 ton of ammonium paratungstate consumes 0.44 tons of liquid ammonia water, and more than 50% of the ammonia is discharged during the process of evaporation, concentration and crystallization, which is called ammonia-containing steam. The principle of the secondary evaporation crystallization of ammonium tungstate mother liquor is the same as the continuous evaporation crystallization of ammonium tungstate, tha...

Claims

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Application Information

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IPC IPC(8): B01D3/14B01D3/32B01D53/18B01D53/14C01C1/12C01C1/10C02F1/20
Inventor 韩正昌王志磊张羽刘大财马军军
Owner NANJING GW ENVIRONMENT ENG
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