CN108840422A - A kind of industrial sewage process method - Google Patents
A kind of industrial sewage process method Download PDFInfo
- Publication number
- CN108840422A CN108840422A CN201810502259.4A CN201810502259A CN108840422A CN 108840422 A CN108840422 A CN 108840422A CN 201810502259 A CN201810502259 A CN 201810502259A CN 108840422 A CN108840422 A CN 108840422A
- Authority
- CN
- China
- Prior art keywords
- parts
- heavy metal
- sewage
- process method
- metal precipitator
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/58—Treatment of water, waste water, or sewage by removing specified dissolved compounds
- C02F1/62—Heavy metal compounds
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/16—Nitrogen compounds, e.g. ammonia
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
- C02F2101/22—Chromium or chromium compounds, e.g. chromates
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Water Treatment By Sorption (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The invention discloses a kind of industrial sewage process methods, including into sewage be added in heavy metal precipitator, stir 30min after stand 60min, after grain slag is separated, then the liquid after separation is filtered;Wherein, the heavy metal precipitator includes the parts by weight of following component:30~40 parts of ferric trichloride, 25~32 parts of milk of lime, 8~12 parts of polyacrylamide, 8~12 parts of sodium hydroxide, 15~21 parts of sepiolite, 5~7 parts of sodium chloride.The present invention, can be by the heavy metal in sewage, ammonia nitrogen substance by the way that heavy metal precipitator is added in sewage;Wherein ferric trichloride, milk of lime, polyacrylamide and sodium hydroxide can be by the heavy metals (the significant heavy element of the bio-toxicities such as mercury (mercury), cadmium, lead, chromium and metalloid arsenic) in sewage, sepiolite and sodium chloride can effectively purify ammonia nitrogen waste water, have high economic benefit.
Description
Technical field
The present invention relates to a kind of industrial sewage process methods, belong to technical field of sewage.
Background technique
Sewage water treatment method includes physical treatment process, method of chemical treatment and biological treatment.Wherein method of chemical treatment is logical
Chemical reaction and effect of mass transmitting are crossed to separate, remove in waste water in dissolving, the pollutant of colloidal state or be translated into harmless
The waste water treatment process of substance.In method of chemical treatment, it is to add the processing unit based on medicament generates chemical reaction:It is mixed
Solidifying, neutralization, redox etc..
Coagulation-settlement process is good with effluent quality compared with other physico-chemical process, process runs well is reliable, warp
It helps the advantages that practical, easy to operate.Its coagulating sedimentation principle is in sedimentation basin by adding some medicaments into water (commonly referred to as
For coagulant and flocculation aid), so that the particle for being difficult to precipitate in water is aggregated with one another and is formed colloid, then with the impurity in water body
In conjunction with the bigger floccule body of formation.Floccule body have powerful adsorption capacity, suspended matter can not only be adsorbed, moreover it is possible to absorbed portion bacterium and
Dissolved matter.Floccule body is increased and is sunk by absorption, volume.
Summary of the invention
The purpose of the present invention is to provide one kind can be by the processing side of the removal of heavy metal, ammonia nitrogen class in trade effluent
Method.
The purpose of the present invention is what is be achieved through the following technical solutions:
A kind of industrial sewage process method, including into sewage be added in heavy metal precipitator, stir 30min after stand
60min after separating grain slag, then is filtered the liquid after separation;Wherein, the heavy metal precipitator includes following component
Parts by weight:30~40 parts of ferric trichloride, 25~32 parts of milk of lime, 8~12 parts of polyacrylamide, 8~12 parts of sodium hydroxide, Hai Pao
15~21 parts of stone, 5~7 parts of sodium chloride.
Further, the heavy metal precipitator includes the parts by weight of following component:35 parts of ferric trichloride, milk of lime 28
Part, 10 parts of polyacrylamide, 10 parts of sodium hydroxide, 18 parts of sepiolite, 6 parts of sodium chloride.
Further, the mass ratio of the sewage and heavy metal precipitator is 1:2~3.
Further, the filtering refers to that the liquid after separation successively passes through sandstone, coarse sand, fine sand, active carbon and biology
Film filtering.
Of the invention has the advantages that:
It (1), can be by the heavy metal in sewage, ammonia nitrogen substance by the way that heavy metal precipitator is added in sewage;Wherein trichlorine
Changing iron, milk of lime, polyacrylamide and sodium hydroxide can be by heavy metal (mercury (mercury), cadmium, lead, chromium and the metalloid in sewage
The significant heavy element of the bio-toxicities such as arsenic), sepiolite and sodium chloride can effectively purify ammonia nitrogen waste water, economic effect with higher
Benefit;
It (2), can various impurity effectively in filter sewage by multiple filtration.
Specific embodiment
Embodiment 1
A kind of heavy metal precipitator provided in this embodiment includes the parts by weight of following component:30 parts of ferric trichloride, lime
25 parts, 8 parts of polyacrylamide, 8 parts of sodium hydroxide, 15 parts of sepiolite, 5 parts of sodium chloride of cream.
Embodiment 2
A kind of heavy metal precipitator provided in this embodiment includes the parts by weight of following component:40 parts of ferric trichloride, lime
32 parts, 12 parts of polyacrylamide, 12 parts of sodium hydroxide, 21 parts of sepiolite, 7 parts of sodium chloride of cream.
Embodiment 3
A kind of heavy metal precipitator provided in this embodiment includes the parts by weight of following component:35 parts of ferric trichloride, lime
28 parts, 10 parts of polyacrylamide, 10 parts of sodium hydroxide, 18 parts of sepiolite, 6 parts of sodium chloride of cream.
Embodiment 4
The present embodiment provides a kind of industrial sewage process method, the huge sum of money provided including embodiment 1 in being added into sewage
The mass ratio of category precipitating reagent, sewage and heavy metal precipitator is 1:3,60min is stood after stirring 30min, after grain slag is separated, then
Liquid after separation is filtered;The filtering refers to that the liquid after separation successively passes through sandstone, coarse sand, fine sand, active carbon
And biofilm filtration.Its solid-liquid separation effect is preferable, settling velocity is fast, and the substance of content of beary metal and ammonia nitrogen class reaches country
Emission request.
Embodiment 5
The present embodiment provides a kind of industrial sewage process method, the huge sum of money provided including embodiment 2 in being added into sewage
The mass ratio of category precipitating reagent, sewage and heavy metal precipitator is 1:2,60min is stood after stirring 30min, after grain slag is separated, then
Liquid after separation is filtered;The filtering refers to that the liquid after separation successively passes through sandstone, coarse sand, fine sand, active carbon
And biofilm filtration.Its solid-liquid separation effect is preferable, settling velocity is fast, and the substance of content of beary metal and ammonia nitrogen class reaches country
Emission request.
Embodiment 6
The present embodiment provides a kind of industrial sewage process method, the huge sum of money provided including embodiment 3 in being added into sewage
The mass ratio of category precipitating reagent, sewage and heavy metal precipitator is 1:2,60min is stood after stirring 30min, after grain slag is separated, then
Liquid after separation is filtered;The filtering refers to that the liquid after separation successively passes through sandstone, coarse sand, fine sand, active carbon
And biofilm filtration.Its good effect of separating solid from liquid, settling velocity are optimum state, and the substance of content of beary metal and ammonia nitrogen class reaches
To national emission request.
The above is only the preferred embodiment of the present invention, but scope of protection of the present invention is not limited thereto, any
The transformation and replacement carried out based on technical solution provided by the present invention and inventive concept should all be covered in protection model of the invention
In enclosing.
Claims (4)
1. a kind of industrial sewage process method, it is characterised in that including heavy metal precipitator in being added into sewage, stir 30min
After stand 60min, after grain slag is separated, then the liquid after separation is filtered;Wherein, the heavy metal precipitator includes such as
The parts by weight of lower component:30~40 parts of ferric trichloride, 25~32 parts of milk of lime, 8~12 parts of polyacrylamide, sodium hydroxide 8~12
Part, 15~21 parts of sepiolite, 5~7 parts of sodium chloride.
2. industrial sewage process method according to claim 1, it is characterised in that:The heavy metal precipitator includes as follows
The parts by weight of component:35 parts of ferric trichloride, 28 parts of milk of lime, 10 parts of polyacrylamide, 10 parts of sodium hydroxide, 18 parts of sepiolite, chlorine
Change 6 parts of sodium.
3. according to claim 1 or industrial sewage process method described in 2 any claims, it is characterised in that:The sewage
Mass ratio with heavy metal precipitator is 1:2~3.
4. industrial sewage process method according to claim 1, it is characterised in that:The filtering refers to the liquid after separation
Successively pass through sandstone, coarse sand, fine sand, active carbon and biofilm filtration.
Priority Applications (1)
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CN201810502259.4A CN108840422A (en) | 2018-05-23 | 2018-05-23 | A kind of industrial sewage process method |
Applications Claiming Priority (1)
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CN201810502259.4A CN108840422A (en) | 2018-05-23 | 2018-05-23 | A kind of industrial sewage process method |
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CN108840422A true CN108840422A (en) | 2018-11-20 |
Family
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CN201810502259.4A Pending CN108840422A (en) | 2018-05-23 | 2018-05-23 | A kind of industrial sewage process method |
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Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR890002277B1 (en) * | 1984-07-13 | 1989-06-27 | 가부시기가이샤 히다찌세이사꾸쇼 | Method of treating liquid waste containing heavy metal chelate compound |
CN103342429A (en) * | 2013-07-30 | 2013-10-09 | 北京矿冶研究总院 | Method for recovering, treating and recycling valuable metals in waste acid |
CN105923842A (en) * | 2016-06-23 | 2016-09-07 | 陈朝民 | Method for removing heavy metal ions in sewage |
CN106809892A (en) * | 2015-11-30 | 2017-06-09 | 周子童 | A kind of production method of sewage-treating agent |
CN107417004A (en) * | 2017-05-19 | 2017-12-01 | 北京中科康仑环境科技研究院有限公司 | A kind of method of advanced treating acid waste water containing thallium |
-
2018
- 2018-05-23 CN CN201810502259.4A patent/CN108840422A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR890002277B1 (en) * | 1984-07-13 | 1989-06-27 | 가부시기가이샤 히다찌세이사꾸쇼 | Method of treating liquid waste containing heavy metal chelate compound |
CN103342429A (en) * | 2013-07-30 | 2013-10-09 | 北京矿冶研究总院 | Method for recovering, treating and recycling valuable metals in waste acid |
CN106809892A (en) * | 2015-11-30 | 2017-06-09 | 周子童 | A kind of production method of sewage-treating agent |
CN105923842A (en) * | 2016-06-23 | 2016-09-07 | 陈朝民 | Method for removing heavy metal ions in sewage |
CN107417004A (en) * | 2017-05-19 | 2017-12-01 | 北京中科康仑环境科技研究院有限公司 | A kind of method of advanced treating acid waste water containing thallium |
Non-Patent Citations (1)
Title |
---|
张玉龙等主编: "《水处理剂配方设计与实例》", 31 May 2011, 中国纺织出版社 * |
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Application publication date: 20181120 |