CN103896457A - Fine chemical wastewater treatment process - Google Patents
Fine chemical wastewater treatment process Download PDFInfo
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- CN103896457A CN103896457A CN201410129246.9A CN201410129246A CN103896457A CN 103896457 A CN103896457 A CN 103896457A CN 201410129246 A CN201410129246 A CN 201410129246A CN 103896457 A CN103896457 A CN 103896457A
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Abstract
The invention discloses a fine chemical wastewater treatment process. The fine chemical wastewater treatment process comprises the following steps of: (1) treating by pre-oxidation, namely, adding wastewater to a floatation tank through an adjusting tank, and then adding an inorganic strong oxide to the floatation tank to treat the wastewater by oxidizing; (2) performing hydrolytic acidification; (3) performing biological treatment, namely, performing biological treatment for the acidified wastewater through an anaerobic tank and an aerobic tank in sequence; (4) treating through activated sludge, namely, treating the wastewater subjected to biological treatment through a mudpack MBBR (Moving Bed Biofilm Reactor) and activated sludge; (5) flocculating and settling, namely, transferring the treated activated sludge into a flocculating and settling tank, then adding 30% of sodium hydroxide to adjust the pH to be 8 to 9, adding 30-4-mg/L of PAC (Poly Aluminium Chloride), and finally adding 70 to 90mg/L of flocculating agent to separate mud and water; and (6) deeply treating, namely, performing rough filtration and fine filtration for the output water in sequence, and then treating by an RO (Reverse Osmosis) film. With the adoption of the fine chemical wastewater treatment process, the biodegradability of wastewater can be improved, organic matters in wastewater can be removed efficiently, the wastewater can be recovered and recycled, and thus the water resource is saved; in addition, the recovery process is short, and the system recovery rate is high.
Description
Technical field
The present invention relates to chemical field, relate in particular to a kind of Fine Chemistry Wastewater treatment process.
Background technology
The waste water producing in fine chemical product production process, organic pollutant content is higher, also there is other feature according to the difference of technique, as high in salt concentration, poisonous, coloring matter content is high, bio-refractory material is many, the features such as waste water bio-degradable is poor, conventional materialization and biochemical treatment are difficult to reach emission request, project completing the standard rate wretched insufficiency for a long time.
Summary of the invention
The object of the invention is to overcome the deficiencies in the prior art, a kind of biodegradability that improves Fine Chemistry Wastewater is provided, remove the organic waste water treatment process in sewage with greater efficiency, waste water is reclaimed and utilized, saving water resource.
The present invention adopts following technical scheme to achieve these goals:
A kind of Fine Chemistry Wastewater treatment process, comprises the following steps:
(1) pre-oxidation treatment: waste water, through equalizing tank, enters air flotation pool, adds inorganic strong oxide compound to carry out wastewater oxidation processing in air flotation pool, and the amount adding is 80-100mg/L, and pretreatment time is 12-15 minute;
(2) acidication: the wastewater from chemical industry after oxide treatment is placed in to the hydrolysis acidification pool acidifying that is hydrolyzed, and hydrolysis time is 4-5 hour;
(3) biological treatment: the waste water after acidifying is carried out a biological disposal upon through anaerobic pond, Aerobic Pond successively;
(4) sludge treatment of invigorating blood circulation: after carrying out a biological disposal upon, waste water is through mud film MBBR and active sludge treatment;
(5) flocculating settling: enter coagulation reaction tank after the sludge treatment of invigorating blood circulation, first add 30% sodium hydroxide to regulate pH value to add PAC to 8-9 and by the consumption of 30-4-mg/L, then add flocculation agent to carry out mud-water separation by the consumption of 70-90mg/L;
(6) advanced treatment: water outlet enters the processing of RO film successively after coarse filtration, essence filter.
Described inorganic strong oxide compound is one or more in sodium chlorate, sodium manganate, Na2Fe04, nickel oxide and cerium oxide.
Described anaerobic pond is UASB anaerobic sludge expansion pond.
Described Aerobic Pond is value aerobic biofilter.
Described flocculation agent be in polymer alumina, polypropylene aminoacyl one or both.
Compared with the prior art, beneficial effect of the present invention is as follows:
The present invention can improve the biodegradability of waste water, removes the organism in sewage with greater efficiency, and device structure is simple, convenient operation and maintenance, reclaim and utilize waste water, saving water resource, have good economy and environment benefit, recovery process flow process is short, and system recoveries rate is high.
Embodiment
Below in conjunction with embodiment, the invention will be further described.
Embodiment 1:
The present embodiment adopts the Fine Chemistry Wastewater of following index:
A kind of Fine Chemistry Wastewater treatment process, comprises the following steps:
(1) pre-oxidation treatment: waste water, through equalizing tank, enters air flotation pool, adds sodium chlorate, sodium manganate, Na2Fe04, nickel oxide and cerium oxide in air flotation pool, carries out wastewater oxidation processing, and the amount adding is 100mg/L, and pretreatment time is 15 minutes;
(2) acidication: the wastewater from chemical industry after oxide treatment is placed in to the hydrolysis acidification pool acidifying that is hydrolyzed, and hydrolysis time is 5 hours;
(3) biological treatment: the waste water after acidifying is carried out a biological disposal upon through UASB anaerobic sludge expansion pond, aerobic biofilter successively;
(4) sludge treatment of invigorating blood circulation: after carrying out a biological disposal upon, waste water is through mud film MBBR and active sludge treatment;
(5) flocculating settling: enter coagulation reaction tank after the sludge treatment of invigorating blood circulation, first add 30% sodium hydroxide adjusting pH value to 8 and add PAC by the consumption of 30mg/L, then add polymer alumina and polypropylene aminoacyl to carry out mud-water separation by the consumption of 80mg/L;
(6) advanced treatment: water outlet enters the processing of RO film successively after coarse filtration, essence filter.
Following table is the treatment effect of this technique to Fine Chemistry Wastewater:
Claims (5)
1. a Fine Chemistry Wastewater treatment process, is characterized in that: comprise the following steps:
(1) pre-oxidation treatment: waste water, through equalizing tank, enters air flotation pool, adds inorganic strong oxide compound to carry out wastewater oxidation processing in air flotation pool, and the amount adding is 80-100mg/L, and pretreatment time is 12-15 minute;
(2) acidication: the wastewater from chemical industry after oxide treatment is placed in to the hydrolysis acidification pool acidifying that is hydrolyzed, and hydrolysis time is 4-5 hour;
(3) biological treatment: the waste water after acidifying is carried out a biological disposal upon through anaerobic pond, Aerobic Pond successively;
(4) sludge treatment of invigorating blood circulation: after carrying out a biological disposal upon, waste water is through mud film MBBR and active sludge treatment;
(5) flocculating settling: enter coagulation reaction tank after the sludge treatment of invigorating blood circulation, first add 30% sodium hydroxide to regulate pH value to add PAC to 8-9 and by the consumption of 30-4-mg/L, then add flocculation agent to carry out mud-water separation by the consumption of 70-90mg/L;
(6) advanced treatment: water outlet enters the processing of RO film successively after coarse filtration, essence filter.
2. fine chemical product waste water treatment process according to claim 1, is characterized in that: described inorganic strong oxide compound is one or more in sodium chlorate, sodium manganate, Na2Fe04, nickel oxide and cerium oxide.
3. fine chemical product waste water treatment process according to claim 1, is characterized in that: described anaerobic pond is UASB anaerobic sludge expansion pond.
4. fine chemical product waste water treatment process according to claim 1, is characterized in that: described Aerobic Pond is aerobic biofilter.
5. fine chemical product waste water treatment process according to claim 1, is characterized in that: described flocculation agent be in polymer alumina, polypropylene aminoacyl one or both.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201410129246.9A CN103896457B (en) | 2014-04-01 | 2014-04-01 | A kind of Fine Chemistry Wastewater treatment process |
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| CN201410129246.9A CN103896457B (en) | 2014-04-01 | 2014-04-01 | A kind of Fine Chemistry Wastewater treatment process |
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| CN103896457A true CN103896457A (en) | 2014-07-02 |
| CN103896457B CN103896457B (en) | 2015-11-04 |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105254117A (en) * | 2015-09-24 | 2016-01-20 | 安庆丰源化工有限公司 | Treatment method of fine chemical engineering oily wastewater |
| CN105819633A (en) * | 2016-05-30 | 2016-08-03 | 安庆丰源化工有限公司 | Method for chemical wastewater treatment |
| CN110357371A (en) * | 2019-08-28 | 2019-10-22 | 杨柳 | A kind of refined processing method of chemical spent material sewage |
| US20230002258A1 (en) * | 2018-05-03 | 2023-01-05 | Headworks Bio, Inc. | Systems and methods for oxidizing disinfectants combined with moving bed biofilm reactors |
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| EP1630139A1 (en) * | 2004-08-23 | 2006-03-01 | Amecon Environmental Consultancy | Process for the biological denitrification of ammonium containing wastewater |
| CN102336502A (en) * | 2011-08-26 | 2012-02-01 | 无锡通源环保技术工程有限公司 | Combination type treatment method for pharmaceutical waste water |
| WO2012075615A1 (en) * | 2010-12-06 | 2012-06-14 | 南京大学 | Integrated bioreactor and use thereof and method for treating high content organic wastewater |
| CN102583879A (en) * | 2012-01-16 | 2012-07-18 | 宁波工程学院 | High-concentration integrated chemical organic wastewater treatment process |
| CN103159381A (en) * | 2013-04-11 | 2013-06-19 | 杭州天创环境科技股份有限公司 | Fine chemical wastewater treatment and reuse method |
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2014
- 2014-04-01 CN CN201410129246.9A patent/CN103896457B/en active Active
Patent Citations (5)
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|---|---|---|---|---|
| EP1630139A1 (en) * | 2004-08-23 | 2006-03-01 | Amecon Environmental Consultancy | Process for the biological denitrification of ammonium containing wastewater |
| WO2012075615A1 (en) * | 2010-12-06 | 2012-06-14 | 南京大学 | Integrated bioreactor and use thereof and method for treating high content organic wastewater |
| CN102336502A (en) * | 2011-08-26 | 2012-02-01 | 无锡通源环保技术工程有限公司 | Combination type treatment method for pharmaceutical waste water |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105254117A (en) * | 2015-09-24 | 2016-01-20 | 安庆丰源化工有限公司 | Treatment method of fine chemical engineering oily wastewater |
| CN105819633A (en) * | 2016-05-30 | 2016-08-03 | 安庆丰源化工有限公司 | Method for chemical wastewater treatment |
| US20230002258A1 (en) * | 2018-05-03 | 2023-01-05 | Headworks Bio, Inc. | Systems and methods for oxidizing disinfectants combined with moving bed biofilm reactors |
| CN110357371A (en) * | 2019-08-28 | 2019-10-22 | 杨柳 | A kind of refined processing method of chemical spent material sewage |
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|---|---|
| CN103896457B (en) | 2015-11-04 |
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