Electroplating comprehensive wastewater zero-discharge treatment system and process thereof

An electroplating integrated and treatment system technology, applied in the field of electroplating integrated wastewater treatment system with zero discharge, can solve the problems of fouling and clogging of the evaporation system, high cost of hazardous waste disposal, and increase the burden on enterprises, so as to reduce fouling, clogging and cost. low, improved evaporation and crystallinity

Pending Publication Date: 2022-06-14
李鹏
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Advanced oxidation is not selective, and it will preferentially oxidize easily oxidizable and easily degradable organic matter in wastewater. Therefore, although the COD value of wastewater treated by advanced oxidation method may be significantly reduced on the surface, there will still be a large amount of refractory organic matter in the wastewater. , these refractory organic substances will be enriched after entering the evaporation system, and will cause problems such as scaling and blockage, large foam volume, and non-crystallization of salt in the evaporation system; single-effect evaporation + drying method, low-temperature evaporation method, and solidification method are all only Concentrating the pollutants in the electroplating wastewater does not treat the pollutants contained in the wastewater. Only a small amount of electroplating wastewater can be transitionally treated, which cannot fundamentally solve the pollution problem of electroplating wastewater; in addition, the above treatment methods still exist With the problems of large equipment investment and high treatment costs, a large amount of hazardous waste will be generated after treatment, and the cost of hazardous waste disposal will be higher, further increasing the burden on enterprises

Method used

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  • Electroplating comprehensive wastewater zero-discharge treatment system and process thereof
  • Electroplating comprehensive wastewater zero-discharge treatment system and process thereof
  • Electroplating comprehensive wastewater zero-discharge treatment system and process thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0039] Step 1: Collect the electroplating integrated wastewater, the PH value of the comprehensive wastewater is 12, the conductivity is 12870 μS / cm, the content of iron ions is 1.2mg / L, the content of copper ions is 1.6mg / L, the content of nickel ions is 1.5mg / L, the content of chromium ions is 529mg / L, and the content of zinc ions is 9500mg / L; COD is 8650mg / L, ammonia nitrogen is 25mg / L, turbidity is 18NTU;

[0040] Step 2: Add 30% hydrochloric acid to the wastewater to adjust the PH value of 8.5, add heavy metal ion trap and flocculant PAM, precipitated sludge with plate and frame filter press filter press, to obtain the filter cake, iron, copper, nickel, chromium, zinc and other heavy metal ions in the wastewater and some organic matter present in the filter cake; The coD of the supernatant and filtrate after physicochemization is 2050mg / L, the ammonia nitrogen is 46mg / L, and the turbidity is 10NTU;

[0041] Step 3: The physicochemical supernatant and filtrate are entered into t...

Embodiment 2

[0053] Step 1: Collect the electroplating integrated wastewater, the PH value of the comprehensive wastewater is 2.3, the conductivity is 35800μS / cm, the content of iron ions is 21000mg / L, the content of copper ions is 8500mg / L, the content of nickel ions is 1560mg / L, the content of chromium ions is 83mg / L, and the content of zinc ions is 9500mg / L; COD is 7580mg / L, ammonia nitrogen is 25mg / L, turbidity is 17NTU;

[0054]Step 2: Add 30% hydrochloric acid to the wastewater to adjust the PH value of 8.5, add heavy metal ion trap and flocculant PAM, precipitated sludge with plate and frame filter press filter press, to obtain the filter cake, iron, copper, nickel, chromium, zinc and other heavy metal ions in the wastewater and some organic matter present in the filter cake; The coD of the supernatant and filtrate after physicochemization is 1560mg / L, the ammonia nitrogen is 65mg / L, and the turbidity is 12NTU;

[0055] Step 3: The filtrate is entered into the biochemical system, and af...

Embodiment 3

[0067] Step 1: Collect the electroplating integrated wastewater, the PH value of the comprehensive wastewater is 3.8, the conductivity is 25500μS / cm, the content of iron ions is 3560mg / L, the content of copper ions is 1690mg / L, the content of nickel ions is 3670mg / L, the content of chromium ions is 95mg / L, and the content of zinc ions is 4580mg / L; COD is 9650mg / L, ammonia nitrogen is 18mg / L, turbidity is 26NTU;

[0068] Step 2: Add 30% hydrochloric acid to the wastewater to adjust the PH value of 8.5, add heavy metal ion trapping agent and flocculant PAM, press the filter with a plate and frame filter press to obtain filtrate and filter cake; the COD of the filtrate is 2950mg / L, the ammonia nitrogen is 18mg / L, and the turbidity is 22NTU; Most of the heavy metal ions such as iron, copper, nickel, chromium, zinc and some organic matter in the wastewater are present in the filter cake;

[0069]Step 3: The filtrate is entered into the biochemical system, and after aerobic, anaerobic a...

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Abstract

The invention provides a treatment system for zero discharge of comprehensive electroplating wastewater and a treatment process thereof. The invention belongs to the technical field of sewage treatment, and relates to a zero-discharge treatment system for comprehensive electroplating wastewater. Comprising a physicochemical system, a biochemical system, a membrane concentration system, a special pretreatment system and an evaporation system which are connected in sequence. According to the invention, the high-salt concentrated water subjected to membrane concentration can be treated by the pretreatment system before entering the evaporation system, so that pollutants influencing evaporation in the high-salt concentrated water are removed, the viscosity of the concentrated water is reduced, the evaporation and crystallinity of the concentrated water are improved, and the concentrated water enters the evaporation crystallization system to obtain a byproduct salt; the evaporated and crystallized mother liquor is returned to the pretreatment system to be mixed with the membrane concentration high-salt concentrated water for circular treatment, pollutants enriched in the mother liquor are removed, and the mother liquor can be continuously evaporated and desalted, so that zero mother liquor of the evaporation system is realized, and zero emission of the electroplating comprehensive wastewater is realized.

Description

technical field [0001] The invention belongs to the technical field of sewage treatment, and relates to a zero-discharge treatment system for comprehensive electroplating wastewater and a process thereof. Background technique [0002] Electroplating is the process of plating a thin layer of other metals or alloys on some metal surfaces by using the principle of electrolysis. It is a commonly used treatment process in industrial production and is widely used in aviation, aerospace, electrical appliances, decorative materials and other industries. Before electroplating, metal parts need to be degreased and derusted with acid and alkali, and then washed with a large amount of water for many times before they can enter the electroplating process; in addition, a plating solution containing heavy metal ions such as chromium, zinc, copper, nickel, etc. is used in the electroplating process. This makes the electroplating industry not only consume a lot of water, but also has a very ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/14C02F103/16
CPCC02F9/00C02F1/66C02F1/62C02F1/56C02F1/24C02F3/30C02F1/444C02F1/441C02F1/58C02F1/04C02F11/122C02F2103/16C02F2209/08C02F2209/14C02F2209/11C02F2301/08C02F2301/046
Inventor 李鹏齐枫楠林健龙
Owner 李鹏
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