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Process for extracting ammonium chloride from waste etching liquid and evaporation and concentration system thereof

An evaporative concentration system and a technology for waste etching solution, which are applied in the field of technology and its evaporative concentration system, can solve the problems of low value and low purity of ammonium chloride, and achieve the effects of improving recovery rate, low energy consumption and good adsorption effect.

Pending Publication Date: 2020-12-29
温州科锐环境资源利用有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] This method has the following defects: due to the removal of ammonium ion (NH 4+ ), chloride ion (CL - ), and unextracted copper ions (Cu 2+ ) and other heavy metal impurities, although a certain amount of ammonium chloride product can be obtained through simple concentration treatment, but the purity of the ammonium chloride product is low, and the selling value is relatively low

Method used

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  • Process for extracting ammonium chloride from waste etching liquid and evaporation and concentration system thereof
  • Process for extracting ammonium chloride from waste etching liquid and evaporation and concentration system thereof
  • Process for extracting ammonium chloride from waste etching liquid and evaporation and concentration system thereof

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Effect test

Embodiment 1

[0039] In order to obtain the higher ammonium chloride product of purity, the application proposes a kind of technique of extracting ammonium chloride from waste etching solution, at least comprises the following steps:

[0040] S1. Filtrating the alkaline waste etching solution to remove suspended impurities and adjusting the pH to 9 to obtain solution a;

[0041] S2. The solution a enters the packed extraction tower for extraction, and the extractant and the diluent with a volume concentration ratio of 4:1 are introduced into the packed extraction tower in advance, and the extraction temperature is set to 10° C. to obtain the organic phase b and the raffinate c;

[0042] S3, adding hydrochloric acid to the raffinate c for conditioning to obtain a solution d;

[0043] S4, in the fixed bed adsorption equipment, adjust the pH value to 4, adopt L-glutamic acid chelating resin to adsorb the heavy metal ion in the solution d for 5min, and obtain the ammonium chloride solution e an...

Embodiment 2

[0056] S1. Filter the alkaline waste etching solution to remove suspended impurities and adjust the pH value to 9.5 to obtain solution a;

[0057] S2. The solution a enters the packed extraction tower for extraction, and the extraction agent and the diluent with a volume concentration ratio of 4:2 are introduced into the packed extraction tower in advance, and the extraction temperature is set to 30° C. to obtain the organic phase b and the raffinate c;

[0058] S3, adding hydrochloric acid to the raffinate c for conditioning to obtain a solution d;

[0059] S4, in the fixed bed adsorption equipment, adjust the pH to be 6, adopt L-glutamic acid chelating resin to adsorb the heavy metal ion in the solution d for 6min, obtain the ammonium chloride solution e and the desorption liquid f;

[0060] S5. Obtain ammonium chloride concentrated solution g by evaporating and concentrating the ammonium chloride solution e, wherein the evaporating and concentrating time is 45 min;

[0061...

Embodiment 3

[0064] S1. Filtrating the alkaline waste etching solution to remove suspended impurities and adjusting the pH value to 10 to obtain solution a;

[0065] S2. The solution a enters the packed extraction tower for extraction, and only imports the extractant of equal concentration into the packed extraction tower in advance, and sets the extraction temperature to 60° C. to obtain the organic phase b and the raffinate c;

[0066] S3, adding hydrochloric acid to the raffinate c for conditioning to obtain a solution d;

[0067] S4, in the fixed bed adsorption equipment, adjust the pH value to be 8, adopt the L-glutamic acid chelating resin to adsorb the heavy metal ion in the solution d for 7min, obtain the ammonium chloride solution e and the desorption liquid f;

[0068] S5. Obtain ammonium chloride concentrated solution g by evaporating and concentrating the ammonium chloride solution e, wherein the evaporating and concentrating time is 60 min;

[0069] S6. Cooling and crystalliz...

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Abstract

The invention discloses a process for extracting ammonium chloride from a waste etching solution and an evaporation and concentration system thereof, and the process comprises the following steps: S1,filtering an alkaline waste etching solution to remove suspended impurities to obtain a solution a, and adjusting the pH value to 9-10; S2, enabling the solution a to enter a filler extraction towerto be extracted, so as to obtain an organic phase b and raffinate c; S3, adding hydrochloric acid into the raffinate c for tempering to obtain a solution d; S4, in fixed bed adsorption equipment, adsorbing heavy metal ions in the solution d by adopting L-glutamic acid chelating resin to obtain an ammonium chloride solution e and a desorption solution f; S5, evaporating and concentrating the ammonium chloride solution e to obtain an ammonium chloride concentrated solution g; and S6, cooling and crystallizing the ammonium chloride concentrated solution g. The evaporation and concentration systemcomprises a liquid feeding device, a negative pressure evaporation device, a condensation device and a condensate water collection device which are connected through pipelines. The method can be applied to waste liquid treatment plants and has the advantage of extracting the purity of ammonium chloride.

Description

technical field [0001] The invention relates to the technical field of ammonium chloride recovery, more specifically, it relates to a process for extracting ammonium chloride from waste etching solution and an evaporation and concentration system thereof. Background technique [0002] Printed circuit board (PCB) is an important part of electronic products. In recent years, with the rapid development of the electronic industry, the demand for PCB is increasing, and the PCB industry has achieved rapid development. With the continuous development of the PCB industry, the environmental protection issues of this industry are becoming more and more important. One of the main pollution is the large amount of copper-containing etching waste produced in the etching process. This waste liquid mainly comes from the PCB etching process. The etching liquid can corrode the excess copper foil on the circuit board, so that the concentration of copper ions in the etching liquid increases con...

Claims

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Application Information

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IPC IPC(8): C01C1/16C02F9/10C02F101/16C02F101/20C02F103/34
CPCC01C1/164C02F9/00C02F1/001C02F1/66C02F1/04C02F1/285C02F1/26C02F1/046C02F2001/5218C02F1/52C02F2101/20C02F2101/16C02F2103/346Y02P10/20
Inventor 麻洪明林小胡何朋朋
Owner 温州科锐环境资源利用有限公司
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