CN107902796A - Pig-farm wastewater advanced treatment process - Google Patents

Pig-farm wastewater advanced treatment process Download PDF

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Publication number
CN107902796A
CN107902796A CN201711145436.XA CN201711145436A CN107902796A CN 107902796 A CN107902796 A CN 107902796A CN 201711145436 A CN201711145436 A CN 201711145436A CN 107902796 A CN107902796 A CN 107902796A
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China
Prior art keywords
pig
farm wastewater
liquid
treatment
sufficiently stirred
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Application number
CN201711145436.XA
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Chinese (zh)
Inventor
林海彬
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Minnan Normal University
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Minnan Normal University
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Priority to CN201711145436.XA priority Critical patent/CN107902796A/en
Publication of CN107902796A publication Critical patent/CN107902796A/en
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/001Processes for the treatment of water whereby the filtration technique is of importance
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/285Treatment of water, waste water, or sewage by sorption using synthetic organic sorbents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5236Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/58Treatment of water, waste water, or sewage by removing specified dissolved compounds
    • C02F1/62Heavy metal compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/66Treatment of water, waste water, or sewage by neutralisation; pH adjustment
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/105Phosphorus compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/16Nitrogen compounds, e.g. ammonia
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/20Heavy metals or heavy metal compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/20Nature of the water, waste water, sewage or sludge to be treated from animal husbandry
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00General aspects of water treatment
    • C02F2301/08Multistage treatments, e.g. repetition of the same process step under different conditions

Abstract

A kind of pig-farm wastewater advanced treatment process, concrete scheme are as follows:Step 1, will be carried out the pig-farm wastewater after biochemical treatment using the prior art and carry out single treatment to it using aluminum chloride flocculant;Step 2, the waste liquid for obtaining step 1 add copper ion complexing agent and carry out complex-precipitation, and specific equation is as follows:Step 3, by step 2 waste liquid by chelating resin chelating realize Absorptive complex wave, realize deep purifying.Pig-farm wastewater its nitrogen content after handling three times is less than 20.0 milligrams/L, and phosphorus content is less than 5.0 milligrams/L, meets relevant emission standards, can directly discharge, avoid the pollution to environment.

Description

Pig-farm wastewater advanced treatment process
Technical field
This patent is related to sewage purification field, espespecially a kind of pig-farm wastewater advanced treatment process.
Background technology
China is the first in the world pig raising big country, and the influence of the development of industry of raising pigs to environment is very big.It is fast with aquaculture Speed development, the high concentration organic contaminant and nitrogen and phosphorus pollution object amount of animal farm wastewater discharge continue to increase, and what is be induced by it is huge Pollution problem is increasingly taken seriously.At present, processing of each pig raising enterprise to pig-farm wastewater at present, is substantially using biochemical process Preliminary processing is carried out, such as:Xue Yu applies《A kind of method using pig farm Pig dung and urine production biogas》(application number: 201611231308.2) and the application such as Shen Qirong《A kind of method of the aquatic production organic fertilizer of recycling pig manure》(application number: 201710076378.3) it is still total containing higher concentration in the waste water after biochemical treatment, but since pig-farm wastewater component is more complicated Nitrogen and total phosphorus, can not directly discharge at all, it is therefore desirable to further advanced treating, to ensure the waste water of pig raising enterprise effluent Middle total nitrogen, total phosphorus are greatly lowered to reach discharge standard.
The content of the invention
The goal of the invention of this patent is to provide a kind of advanced treatment process of pig-farm wastewater, to meet discharge standard, Reduce pollution.
A kind of pig-farm wastewater advanced treatment process, concrete scheme are as follows:
Step 1, will be carried out the pig-farm wastewater after biochemical treatment using the prior art it carried out using aluminum chloride flocculant Single treatment;
Step 2, the waste liquid for obtaining step 1 add copper ion complexing agent and carry out complex-precipitation, and specific equation is as follows:
Step 3, by step 2 waste liquid Absorptive complex wave is realized by chelating resin chelating, realize deep purifying, specific side Formula is as follows:
A kind of above-described pig-farm wastewater advanced treatment process, its further scheme are:
Step 1, the ratio by the pig-farm wastewater after utilization prior art biochemical treatment according to every liter of addition 0.02g-0.12g After addition aluminum chloride flocculant is sufficiently stirred, filter up to single treatment liquid;
Step 2, the ratio addition copper chloride network by the single treatment liquid that step 1 obtains according to every liter of addition 0.1g-0.6g Mixture, after being sufficiently stirred, is adjusted pH value to 8.0-10.5 with the sodium hydroxide solution of 1.0mol/L, makes wherein have precipitation to analyse Go out, then proceed to stirring 30-60 minutes, filtering, up to after-treatment liquid;
Step 3, by step 2 after-treatment liquid, with the hydrochloric acid solution of 1.0mol/L by the pH value of waste water adjust to 4.0-7.0, adds copper chloride, after being sufficiently stirred, liquid passes through chelating resin according still further to the ratio of every liter of addition 0.04g-0.2g Chelating, then can be achieved the advanced treating of pig-farm wastewater, reach emission request.
This technique has the advantage that:(1) since the pig-farm wastewater after biochemical treatment is more muddy and contains partial polymer, adopt Single treatment is carried out to it with aluminum chloride flocculant;(2) after carrying out single treatment to the pig-farm wastewater after biochemical treatment, in waste water Main component is nitrogenous, phosphorus compound and a small amount of metal ion, since part is nitrogenous, phosphorus compound has stronger coordination spy Property.Therefore, this technology is based on complex-precipitation principle and carries out after-treatment to pig-farm wastewater;(3) secondary place is carried out to pig-farm wastewater After reason, the weaker nitrogenous, phosphorus compound of part coordination ability and a small amount of metal ion are contained in waste water.Therefore, this technology is with chela Resin is sorbing material, and pig-farm wastewater is handled three times based on Absorptive complex wave principle.Pig after handling three times Its nitrogen content of excrement waste water is less than 20.0 milligrams/L, and phosphorus content is less than 5.0 milligrams/L, meets relevant emission standards, can directly arrange Put, avoid the pollution to environment.
Embodiment
Embodiment one:A kind of pig-farm wastewater advanced treatment process, its further scheme are:
(1) pig-farm wastewater after 50L prior art biochemical treatments is taken, 1.0 grams of aluminum chloride flocculants is added, is sufficiently stirred Afterwards, filter, up to single treatment liquid.
(2) 5.0 grams of copper chloride is added into single treatment liquid, it is molten with the sodium hydroxide of 1.0mol/L after being sufficiently stirred Liquid adjusts the pH value of waste water to 8.0, makes have Precipitation in waste water, then proceedes to stirring 30 minutes, filtering, up to secondary place Manage liquid.
(3) pH value of after-treatment liquid is adjusted to 4.0 with the hydrochloric acid solution of 1.0mol/L, adds about 2.0 grams of chlorine Change copper, after being sufficiently stirred, by waste water by chelating resin, that is, obtain the pig-farm wastewater after advanced treating.
It is respectively by the pig-farm wastewater measurement wherein the content of nitrogen and phosphorous after advanced treating --- nitrogen content is 16.0 milligrams/L, Phosphorus content is 4.5 milligrams/L)
Embodiment two:A kind of pig-farm wastewater advanced treatment process, its further scheme are:
(1) pig-farm wastewater after 50L prior art biochemical treatments is taken, 2.0 grams of aluminum chloride flocculants is added, is sufficiently stirred Afterwards, filter, up to single treatment liquid.
(2) 15.0 grams of copper chloride is added into single treatment liquid, it is molten with the sodium hydroxide of 1.0mol/L after being sufficiently stirred Liquid adjusts the pH value of waste water to 9.0, makes have Precipitation in waste water, then proceedes to stirring 50 minutes, filtering, up to secondary place Manage liquid.
(3) pH value of after-treatment liquid is adjusted to 5.0 with the hydrochloric acid solution of 1.0mol/L, adds about 5.0 grams of chlorine Change copper, after being sufficiently stirred, by waste water by chelating resin, that is, obtain the pig-farm wastewater after advanced treating.
It is respectively by the pig-farm wastewater measurement wherein the content of nitrogen and phosphorous after advanced treating --- nitrogen content is 14.6 milligrams/L, Phosphorus content is 3.8 milligrams/L)
Embodiment three:A kind of pig-farm wastewater advanced treatment process, its further scheme are:
(1) pig-farm wastewater after 50L prior art biochemical treatments is taken, 4.0 grams of aluminum chloride flocculants is added, is sufficiently stirred Afterwards, filter, up to single treatment liquid.
(2) 25.0 grams of copper chloride is added into single treatment liquid, it is molten with the sodium hydroxide of 1.0mol/L after being sufficiently stirred Liquid adjusts the pH value of waste water to 10.0, makes have Precipitation in waste water, then proceedes to stirring 60 minutes, filtering, up to secondary Treatment fluid.
(3) pH value of after-treatment liquid is adjusted to 6.0 with the hydrochloric acid solution of 1.0mol/L, adds about 8.5 grams of chlorine Change copper, after being sufficiently stirred, by waste water by chelating resin, that is, obtain the pig-farm wastewater after advanced treating.
It is respectively by the pig-farm wastewater measurement wherein the content of nitrogen and phosphorous after advanced treating --- nitrogen content is 12.0 milligrams/L, Phosphorus content is 2.6 milligrams/L)
Example IV:A kind of pig-farm wastewater advanced treatment process, its further scheme are:
(1) pig-farm wastewater after 50L prior art biochemical treatments is taken, 6.0 grams of aluminum chloride flocculants is added, is sufficiently stirred Afterwards, filter, up to single treatment liquid.
(2) 30.0 grams of copper chloride is added into single treatment liquid, it is molten with the sodium hydroxide of 1.0mol/L after being sufficiently stirred Liquid adjusts the pH value of waste water to 10.5, makes have Precipitation in waste water, then proceedes to stirring 30 minutes, filtering, up to secondary Treatment fluid.
(3) pH value of after-treatment liquid is adjusted to 7.0 with the hydrochloric acid solution of 1.0mol/L, adds about 10.0 grams of chlorine Change copper, after being sufficiently stirred, by waste water by chelating resin, that is, obtain the pig-farm wastewater after advanced treating.
It is respectively by the pig-farm wastewater measurement wherein the content of nitrogen and phosphorous after advanced treating --- nitrogen content is 9.0 milligrams/L, phosphorus Content is 1.3 milligrams/L).

Claims (2)

1. a kind of pig-farm wastewater advanced treatment process, concrete scheme are:
Step 1, will be carried out the pig-farm wastewater after biochemical treatment using the prior art it carried out once using aluminum chloride flocculant Processing;
Step 2, the waste liquid for obtaining step 1 add copper ion complexing agent and carry out complex-precipitation, and specific equation is as follows:
Step 3, by step 2 waste liquid by chelating resin chelating realize Absorptive complex wave, realize deep purifying, specific equation It is as follows:
2. a kind of pig-farm wastewater advanced treatment process as claimed in claim 1, its further scheme are:
Step 1, will be added using the pig-farm wastewater after prior art biochemical treatment according to the ratio of every liter of addition 0.02g-0.12g After aluminum chloride flocculant is sufficiently stirred, filter up to single treatment liquid;
Step 2, the ratio addition copper chloride complexing agent by the single treatment liquid that step 1 obtains according to every liter of addition 0.1g-0.6g, After being sufficiently stirred, pH value is adjusted to 8.0-10.5 with the sodium hydroxide solution of 1.0mol/L, makes wherein have Precipitation, then Continue stirring 30-60 minutes, filtering, up to after-treatment liquid;
Step 3, by step 2 after-treatment liquid, the pH value of waste water is adjusted to 4.0- with the hydrochloric acid solution of 1.0mol/L 7.0, copper chloride is added according still further to the ratio of every liter of addition 0.04g-0.2g, after being sufficiently stirred, liquid is chelated by chelating resin, The advanced treating of pig-farm wastewater then can be achieved, reach emission request.
CN201711145436.XA 2017-11-17 2017-11-17 Pig-farm wastewater advanced treatment process Withdrawn CN107902796A (en)

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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102674589A (en) * 2012-04-18 2012-09-19 漳州师范学院 Treatment method of N-phosphonomethyl aminodiacetic acid wastewater
CN103351070A (en) * 2013-07-26 2013-10-16 闽南师范大学 Method for treating glyphosate waste water
CN105217864A (en) * 2015-09-25 2016-01-06 浙江奇彩环境科技有限公司 The treatment process of two cyanogen front-end volatiles waste water in Disperse Blue-60 production process

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102674589A (en) * 2012-04-18 2012-09-19 漳州师范学院 Treatment method of N-phosphonomethyl aminodiacetic acid wastewater
CN103351070A (en) * 2013-07-26 2013-10-16 闽南师范大学 Method for treating glyphosate waste water
CN105217864A (en) * 2015-09-25 2016-01-06 浙江奇彩环境科技有限公司 The treatment process of two cyanogen front-end volatiles waste water in Disperse Blue-60 production process

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
华南农业大学: "《规模化猪场用水与废水处理技术》", 30 June 1996, 中国农业出版社 *
李孟: "《给水处理原理》", 31 December 2013, 武汉理工大学出版社 *
章耀武: "《公知药用基础化学》", 31 May 2012, 人民医院出版社 *
赖日坤: "浅析PCB废水中络合态铜的处理方法", 《中国环保产业》 *

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Application publication date: 20180413