CN106698805A - Energy-saving technology process of sewage treatment - Google Patents
Energy-saving technology process of sewage treatment Download PDFInfo
- Publication number
- CN106698805A CN106698805A CN201510785562.6A CN201510785562A CN106698805A CN 106698805 A CN106698805 A CN 106698805A CN 201510785562 A CN201510785562 A CN 201510785562A CN 106698805 A CN106698805 A CN 106698805A
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- Prior art keywords
- tank
- waste water
- wastewater
- sending
- energy
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Classifications
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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
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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
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
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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
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
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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
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
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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
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
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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
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- 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
- C02F2001/007—Processes including a sedimentation step
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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
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
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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
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
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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
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/28—Anaerobic digestion processes
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)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The invention relates to an energy-saving technology process of sewage treatment, and relates to the technical field of sewage treatment. The energy-saving technology process is characterized by comprising the following steps of firstly, collecting heavy metal-containing wastewater through a pipeline, sending into a grid channel, and enabling the wastewater to pass through a coarse grid; sending the wastewater filtered by the coarse grid into a water collection well, pressurizing the wastewater in the water collection well by a pump, and lifting into a conditioning tank; stirring by a submersible stirrer mounted in the conditioning tank, sending the wastewater stirred in the conditioning tank into a pH (potential of hydrogen) conditioning tank through a lifting pump, and sending the wastewater in the pH conditioning tank into a coagulation reaction tank; sending the wastewater in the coagulation reaction tank into a primary settling tank for primarily settling, enabling supernatant in the primary settling tank to flow into an A/O biochemical tank, decomposing the wastewater in the A/O biochemical tank, and sending into a secondary settling tank; sending the supernatant, subjected to secondary settling, in the secondary settling tank into an intermediate tank, lifting the wastewater in the intermediate tank into an activated carbon tank by a pump, sending the wastewater, subjected to activated carbon adsorption, into a disinfection tank, and disinfecting by the disinfection tank. The energy-saving technology process has the advantages that the environment-friendly and energy-saving effects are realized, the operation process is simple, and the treatment effect is obvious.
Description
Technical field
The present invention relates to technical field of sewage, and in particular to a kind of energy-conservation energy-conservation work of sewage disposal
Skill flow.
Background technology
Sewage disposal:It is to make sewage reach a certain water body of draining or the water quality requirement for reusing and right
Its process for being purified.Sewage disposal is widely used in building, agricultural, traffic, the energy, stone
The every field such as change, environmental protection, urban landscape, medical treatment, food and drink, also come into ordinary hundred more and more
The daily life of surname.Classify by sewage source, sewage disposal is generally divided into production wastewater treatment and life
Sewage disposal.Production waste is dirty by water including trade effluent, rural sewage and medical sewage etc.
Matter is divided, and the pollution of water has two classes:One class is natural pollution;Another kind of is artificial pollution.It is current right
It is artificial pollution that water body endangers larger.Water pollution can according to pollution impurity difference and being broadly divided into
Learn contact scar, physical pollution and biologic contamination three major types.Pollutant mainly has:(1) it is unprocessed
And the industrial wastewater for discharging;(2) it is unprocessed and discharge sanitary sewage;(3) largely using chemical fertilizer,
The farmland sewage of agricultural chemicals, herbicide;(4) trade waste and house refuse by the river is stacked;(5)
Soil erosion;(6) mine system engineering.
The method for processing sewage is a lot, can typically be summarized as Physical, chemical method and bioanalysis etc..
In the epoch that now grows prosperity in heavy industry, increasing heavy metal, the discharge of toxic material are got over
Come more, without treatment, can seriously exceed national standard, can be lived to the producer, periphery
And whole earth zone carrys out inconceivable trouble, due to the treatment such as waste water, sewage belong to high energy consumption,
A kind of inefficient mode, brings financial burden can thus to many enterprises, but if do not locate
Reason problem is more serious, can thus make the orientation direction vicious circle of enterprise.
The content of the invention
The technical problems to be solved by the invention be overcome existing technological deficiency provide a kind of environmental protection,
Energy-conservation, operating process are simple, a kind of energy-conservation energy-conservation technological process of sewage disposal of obvious processing effect.
The technical problems to be solved by the invention are realized using following technical scheme:
A kind of energy-conservation energy-conservation technological process of sewage disposal, it is characterised in that:Including following methods step,
(1) waste water containing heavy metal is collected through piping, into grid canal, by coarse rack, is gone
The larger suspended particulate substance of particle diameter in water removal;
(2) waste water after coarse rack is filtered is put into sump;
(3) supercharging that the waste water in sump is passed through into pump, by waste water lifting to regulating reservoir;
(4) submersible agitator by being installed in regulating reservoir is stirred, and waste water is realized that homogeneous is measured;
(5) waste water stirred in regulating reservoir is entered into PH regulating reservoirs by elevator pump;
(6) in PH regulating reservoirs adding NaOH solution improves the pH value of waste water;
(7) waste water in PH regulating reservoirs is sent into coagulation reaction tank, Fe systems is added in coagulation reaction tank
Flocculant improves the settleability of waste water;
(8) waste water of Fe based flocculating agents will be added to deliver to preliminary sedimentation tank carries out preliminary sedimentation;
(9) supernatant in preliminary sedimentation tank is made to flow to A/0 biochemistry pools certainly;
(10) waste water is in A/0 biochemistry pools, successively anaerobism, it is aerobic under conditions of, by microorganism
Decomposition, degradation go water removal in organic matter;
(11) waste water after decomposition is passed through in second pond, mud-water separation is carried out again;
(12) by the supernatant feeding intermediate pool in the pond after secondary precipitation;
(13) waste water of intermediate pool is lifted in charcoal canister by pump, is made by the absorption of activated carbon
With the heavy metal further gone in water removal;
(14) sterilization pool will be sent into by the waste water after charcoal absorption, is sterilized by sterilization pool, to
Extraneous qualified discharge.
Beneficial effects of the present invention are:The present invention be capable of will regenerate lead bullion, lead bullion, alloy lead,
The road when heavy metal-containing waste water, sanitary sewage, the rainy season that are produced in the production process such as lead oxide and battery
Road rainwater, treatment are clean, reach discharge standard, it is ensured that the reduction of pollution, serve the work of environmental protection
With.Environmental protection of the invention, energy-conservation, operating process are simple, treatment effect is aobvious.
In addition to objects, features and advantages described above, also other purposes of the invention,
Feature and advantage.Below with reference to figure, the present invention is further detailed explanation.
Brief description of the drawings
The accompanying drawing for constituting the part of the application is used for providing a further understanding of the present invention, the present invention
Schematic description and description be used for explain the present invention, do not constitute inappropriate limitation of the present invention.
Fig. 1 is process chart of the invention.
Specific embodiment
In order to make the purpose , technical scheme and advantage of the present invention be clearer, below in conjunction with accompanying drawing
And embodiment, the present invention will be described in further detail.It should be appreciated that described herein specific
Embodiment is only used to explain the present invention, is not intended to limit the present invention.
As shown in figure 1, a kind of energy-conservation energy-conservation technological process of sewage disposal, its method and step is,
(1) waste water containing heavy metal is collected through piping, into grid canal, by coarse rack, is gone
The larger suspended particulate substance of particle diameter in water removal;
(2) waste water after coarse rack is filtered is put into sump;
(3) supercharging that the waste water in sump is passed through into pump, by waste water lifting to regulating reservoir;
(4) submersible agitator by being installed in regulating reservoir is stirred, and waste water is realized that homogeneous is measured;
(5) waste water stirred in regulating reservoir is entered into PH regulating reservoirs by elevator pump;
(6) in PH regulating reservoirs adding NaOH solution improves the pH value of waste water;
(7) waste water in PH regulating reservoirs is sent into coagulation reaction tank, Fe systems is added in coagulation reaction tank
Flocculant improves the settleability of waste water;
(8) waste water of Fe based flocculating agents will be added to deliver to preliminary sedimentation tank carries out preliminary sedimentation;
(9) supernatant in preliminary sedimentation tank is made to flow to A/0 biochemistry pools certainly;
(10) waste water is in A/0 biochemistry pools, successively anaerobism, it is aerobic under conditions of, by microorganism
Decomposition, degradation go water removal in organic matter;
(11) waste water after decomposition is passed through in second pond, mud-water separation is carried out again;
(12) by the supernatant feeding intermediate pool in the pond after secondary precipitation;
(13) waste water of intermediate pool is lifted in charcoal canister by pump, is made by the absorption of activated carbon
With the heavy metal further gone in water removal;
(14) sterilization pool will be sent into by the waste water after charcoal absorption, is sterilized by sterilization pool, to
Extraneous qualified discharge.
Presently preferred embodiments of the present invention is the foregoing is only, is not intended to limit the invention, it is all in this hair
Within bright spirit and principle, any modification, equivalent substitution and improvements made etc. should be included in
Within protection scope of the present invention.
Claims (1)
1. the energy saving technique flow of a kind of sewage disposal, it is characterised in that:Including following methods step,
Waste water containing heavy metal is collected through piping, by grid canal, by coarse rack, removal
The larger suspended particulate substance of particle diameter in water;
Waste water after coarse rack is filtered is put into sump;
The supercharging that waste water in sump is passed through into pump, by waste water lifting to regulating reservoir;
Stirred by the submersible agitator installed in regulating reservoir, waste water is realized that homogeneous is measured;
Waste water stirred in regulating reservoir is entered into PH regulating reservoirs by elevator pump;
NaOH solution is added in PH regulating reservoirs to improve the pH value of waste water;
Waste water in PH regulating reservoirs is sent into coagulation reaction tank, Fe systems wadding is added in coagulation reaction tank
Agent is coagulated to improve the settleability of waste water;
The waste water of Fe based flocculating agents will be added to deliver to preliminary sedimentation tank carries out preliminary sedimentation;
The supernatant in preliminary sedimentation tank is set to flow to A/0 biochemistry pools certainly;
Waste water in A/0 biochemistry pools, successively anaerobism, it is aerobic under conditions of, by microorganism point
The organic matter that solution, degradation are gone in water removal;
Waste water after decomposition is passed through in second pond, mud-water separation is carried out again;
By in the supernatant feeding intermediate pool in the pond after secondary precipitation;
The waste water of intermediate pool is lifted in charcoal canister by pump, is entered by the suction-operated of activated carbon
The heavy metal that one step is gone in water removal.
Priority Applications (1)
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CN201510785562.6A CN106698805A (en) | 2015-11-16 | 2015-11-16 | Energy-saving technology process of sewage treatment |
Applications Claiming Priority (1)
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CN201510785562.6A CN106698805A (en) | 2015-11-16 | 2015-11-16 | Energy-saving technology process of sewage treatment |
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Publication Number | Publication Date |
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CN106698805A true CN106698805A (en) | 2017-05-24 |
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CN201510785562.6A Pending CN106698805A (en) | 2015-11-16 | 2015-11-16 | Energy-saving technology process of sewage treatment |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107417042A (en) * | 2017-08-07 | 2017-12-01 | 江苏天诺环境工程技术开发有限公司 | A kind of industrial sewage treatment technology |
CN110255816A (en) * | 2019-06-17 | 2019-09-20 | 浮山县污水处理厂 | A kind of water inlet NH3- N far surpasses improvement biological denitrification process when design influent quality |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102372400A (en) * | 2011-09-27 | 2012-03-14 | 北京机电院高技术股份有限公司 | Hazardous waste handling center waste water integrated treatment system and method |
CN102826711A (en) * | 2012-08-23 | 2012-12-19 | 安徽省华鑫铅业集团有限公司 | Energy-saving and environmental-protection process flow of sewage treatment |
-
2015
- 2015-11-16 CN CN201510785562.6A patent/CN106698805A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102372400A (en) * | 2011-09-27 | 2012-03-14 | 北京机电院高技术股份有限公司 | Hazardous waste handling center waste water integrated treatment system and method |
CN102826711A (en) * | 2012-08-23 | 2012-12-19 | 安徽省华鑫铅业集团有限公司 | Energy-saving and environmental-protection process flow of sewage treatment |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107417042A (en) * | 2017-08-07 | 2017-12-01 | 江苏天诺环境工程技术开发有限公司 | A kind of industrial sewage treatment technology |
CN110255816A (en) * | 2019-06-17 | 2019-09-20 | 浮山县污水处理厂 | A kind of water inlet NH3- N far surpasses improvement biological denitrification process when design influent quality |
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Application publication date: 20170524 |