CN112607960B - Optimization and improvement method for biochemical treatment load in wastewater treatment - Google Patents

Optimization and improvement method for biochemical treatment load in wastewater treatment Download PDF

Info

Publication number
CN112607960B
CN112607960B CN202011358307.0A CN202011358307A CN112607960B CN 112607960 B CN112607960 B CN 112607960B CN 202011358307 A CN202011358307 A CN 202011358307A CN 112607960 B CN112607960 B CN 112607960B
Authority
CN
China
Prior art keywords
wastewater
section
aeration
aerobic tank
water
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.)
Active
Application number
CN202011358307.0A
Other languages
Chinese (zh)
Other versions
CN112607960A (en
Inventor
陈喜巧
苗兵义
莫利明
张权应
霍保明
范军晓
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SHANXI COKING CO Ltd
Original Assignee
SHANXI COKING CO Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by SHANXI COKING CO Ltd filed Critical SHANXI COKING CO Ltd
Priority to CN202011358307.0A priority Critical patent/CN112607960B/en
Publication of CN112607960A publication Critical patent/CN112607960A/en
Application granted granted Critical
Publication of CN112607960B publication Critical patent/CN112607960B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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
    • C02F1/24—Treatment of water, waste water, or sewage by flotation
    • 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
    • C02F1/5281—Installations for water purification using chemical agents
    • 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
    • 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
    • C02F2101/101—Sulfur compounds
    • 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
    • C02F2101/18—Cyanides
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/001—Upstream control, i.e. monitoring for predictive control
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/06—Controlling or monitoring parameters in water treatment pH
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/07—Alkalinity
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/11—Turbidity
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/40—Liquid flow rate
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00—General aspects of water treatment
    • C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
    • 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
    • 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
    • C02F3/30—Aerobic and anaerobic processes
    • 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
    • C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00—Technologies for wastewater treatment
    • Y02W10/10—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)
  • Activated Sludge Processes (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

The invention discloses an optimization and improvement method for biochemical treatment load in wastewater treatment, and belongs to the field of wastewater treatment. A method for optimizing and improving biochemical treatment load in wastewater treatment comprises the following steps: the wastewater to be treated is sent into an aerobic tank, biological agents are put into the aerobic tank, an air flotation device is arranged in the aerobic tank, the air flotation device is divided into two sections, the first section is an aeration section, a perforated aeration pipe is laid at the bottom of the aeration pipe, aeration holes with the diameter of 1.8-2.2mm are formed in the aeration pipe, the second section is a dosing section for adding flocculating agents and coagulants, the aerobic Chi Jiandu is controlled to be 400-600mg/l, and the reflux ratio of nitrifying liquid is controlled to be 3:1, controlling the content of the thiocyanide in the inlet water of the regulating reservoir to be below 1000 mg/l. The invention can obviously improve the quality of biochemical effluent and the treated water amount, reduce the system operation pressure and save water resources.

Description

Optimization and improvement method for biochemical treatment load in wastewater treatment
Technical Field
The invention relates to the technical field of wastewater treatment, in particular to a method for optimizing and improving biochemical treatment load in wastewater treatment.
Background
The wastewater treatment is to treat wastewater by physical, chemical and biological methods, so that the wastewater is purified, the pollution is reduced, the wastewater is recycled and reused, water resources are fully utilized, and the biochemical treatment is a common treatment mode in the wastewater treatment.
The total treated water quantity of biochemical treatment in the existing wastewater treatment is low, the production requirement is not met, meanwhile, the quality of biochemical effluent water is poor, the cleaning frequency of a deep treatment membrane is increased, the yield of desalted water is low, the impact load resistance capacity of a biological system is poor, dilution water needs to be added in the intermediate process, the concentration of biological contact organic matters is reduced, the water quantity of the system is increased, after the water quality of future water fluctuates, the system is disordered, the effluent water seriously exceeds the standard, the regulation and recovery period is long, the COD of the integral effluent water is higher by 180-200mg/l, the turbidity is 30NTU, the cleaning frequency of a wastewater deep treatment device is caused, the backwashing water quantity is large, the membrane operation period is short, the yield of desalted water is low, the recovery rate is low, and meanwhile, the treated water quantity needs to be reduced for regulation during the disordered regulation period of the system, the vacancy of a regulation pool is reduced, and the regulation and the buffering allowance is insufficient.
Disclosure of Invention
The invention aims to provide a method for optimizing and improving biochemical treatment load in wastewater treatment, so as to solve the problems that the total treatment water amount is low, the production requirement is not met, and the impact load resistance of a biological system is poor in the background technology.
In order to achieve the purpose, the invention provides the following technical scheme:
a method for optimizing and improving biochemical treatment load in wastewater treatment comprises the following steps: the wastewater to be treated is sent into an aerobic tank, biological agents are put into the aerobic tank, an air flotation device is arranged in the aerobic tank, the air flotation device is divided into two sections, the first section is an aeration section, a perforated aeration pipe is laid at the bottom of the aeration pipe, aeration holes with the diameter of 1.8-2.2mm are formed in the aeration pipe, the second section is a dosing section for adding flocculating agents and coagulants, the aerobic Chi Jiandu is controlled to be 400-600mg/l, and the reflux ratio of nitrifying liquid is controlled to be 3:1, controlling the content of the thiocyanide in the inlet water of the regulating reservoir to be below 1000 mg/l.
Furthermore, the traditional air flotation device adopts air flotation at two ends, is modified into first-stage air flotation for removing light oil, and is characterized in that a perforated aeration pipe is laid at the bottom of the first stage of air flotation for continuous aeration and release of bubbles of 2mm, and the light oil floats upwards and is scraped to remove slag; the second section adds drugs to carry out coagulation reaction, and does not carry out aeration and precipitation to carry out slag discharge.
The efficient biological agent adopted by the auxiliary additive is a composite biological agent obtained by combining a plurality of bacillus screened from nature and a single pseudomonas and combining an enzyme preparation prepared from protease, lipase, amylase, urease, cellulase and nitrate reductase in a reasonable proportion, and has a good COD removing effect on the whole, a flocculating agent adopted by the auxiliary additive is an inorganic high-molecular flocculating agent, a coagulating agent adopted by the auxiliary additive is inorganic high-molecular polyaluminium chloride, and the whole performance-price ratio is high.
The ammonia nitrogen regulation index of the aerobic tank is increased, the PH value is controlled to be about 8 when ammonia nitrogen is removed, the PH value is replaced by introducing alkalinity control, and the alkalinity is controlled to be 400-600mg/l, so that the efficient implementation of the nitration reaction can be ensured.
The flocculant is an inorganic polymeric flocculant, and the coagulant is inorganic polymeric polyaluminium chloride.
The main facilities and liquid of the invention comprise an aerobic tank, an anoxic tank, a secondary sedimentation tank, an air flotation device, a biological system, a wastewater sampling inspection system and an auxiliary additive, wherein the whole aerobic tank is of a tank-type container structure and is a core facility of the method, the air flotation device improves the original two-end aeration into a first-stage aeration, a second-stage dosing inspection, a sludge reflux flowmeter, an anoxic tank water inlet flowmeter and a residual sludge discharge flowmeter are arranged in the biological system, the sampling device and the wastewater detection device are main equipment in the wastewater sampling inspection system, and the auxiliary additive adopts a high-efficiency biological agent, a flocculating agent and a coagulant.
Specifically, the variety of the flora is increased, the activity of the flora is enhanced, the efficient biological agent is added into an aerobic tank of a key core facility, and the activity of the biological flora is improved by introducing various biological floras, so that the degradation of the microorganisms on organic matters in the wastewater is more efficient, the nitration reaction rate is improved, the organic matters are efficiently removed in the biological stage, and the adding amount of subsequent chemical agents is reduced; performing water quality detection operation, performing a flocculation reagent adding test for multiple times according to water quality, and selecting a high-efficiency and economical reagent, wherein the effluent is light in color and the turbidity is stable at 10NTU; the improved air floatation device is utilized to carry out normal use work, and organic matters are reduced from the source; the sludge reflux flowmeter, the anoxic tank water inlet flowmeter and the excess sludge discharge flowmeter are additionally arranged in a biological treatment stage, so that eyes are added in a biological system, the flow of sludge and the reflux quantity of supernatant in a secondary sedimentation tank are adjusted in time after the quality of water in the incoming water fluctuates, the index of the biological system is guaranteed, and the excess sludge is discharged in time according to the system operation and the sludge condition, so that microbial flora in the sludge is kept in a logarithmic growth period, and higher sludge activity is kept; through wastewater monitoring, the dosage is increased in time at the air flotation source, organic matters are reduced, the water quality entering a biochemical system is stabilized, and the fluctuation impact of the water quality is avoided; optimizing indexes, increasing the alkalinity analysis indexes of the aerobic tank, controlling the alkalinity of the aerobic tank to be 400-600mg/l, and controlling the reflux ratio of nitrifying liquid to be 3:1, controlling the content of thiocyanide in the inlet water of the regulating reservoir to be below 1000 mg/l.
Compared with the prior art, the invention has the beneficial effects that: through reforming transform the source preliminary treatment air supporting device, scrape the sediment with the light oil come-up and get rid of, then add the medicine and carry out coagulation reaction, sediment is arranged to the non-aeration sediment, the organic matter has been reduced from the source, and through increasing the flora kind, strengthen the flora activity, make the microorganism to the degradation of organic matter in the waste water more high-efficient, improve the nitration rate, high-efficient organic matter of getting rid of in biological phase, reduce the input volume of follow-up chemical agent, make the microorganism flora keep in the mud in the logarithmic growth period, keep higher mud activity, thereby realize biochemical effluent quality of water improvement, the treatment water yield improves, make the condition of restricting coking and dry quenching coking operation obtain the effect of greatly improving, furthest's optimization waste water system is balanced, can alleviate the operating pressure of follow-up waste water advanced treatment membrane device in the whole processing procedure, prolong membrane life, improve the product water recovery rate, practice thrift the water resource.
In conclusion, the invention can obviously improve the quality of biochemical effluent and the quantity of treated water, reduce the operation pressure of the system and save water resources.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be obtained by a person skilled in the art without making any creative effort based on the embodiments in the present invention, belong to the protection scope of the present invention.
Example one
The method for optimizing and improving the biochemical treatment load in the wastewater treatment is realized by the following steps:
the method comprises the following steps: increasing the variety of floras to enhance the activity of the floras, adding 460t of high-efficiency biological agents into an aerobic tank of a key core facility, introducing various biological floras and improving the activity of the biological floras, so that the degradation of microorganisms on organic matters in wastewater is more efficient, the nitration reaction rate is improved, the organic matters are efficiently removed in a biological stage, and the adding amount of subsequent chemical agents is reduced;
step two: performing water quality detection operation, performing a flocculation reagent adding test for multiple times according to water quality, and selecting a high-efficiency and economic reagent, wherein the effluent is light in color and the turbidity is stabilized at 10NTU;
step three: the improved primary air floatation device is utilized to carry out normal use work, and organic matters are reduced from the source;
step four: the sludge reflux flowmeter, the anoxic tank water inlet flowmeter and the excess sludge discharge flowmeter are additionally arranged in a biological treatment stage, so that eyes are added in a biological system, the flow of sludge and the reflux quantity of supernatant of a secondary sedimentation tank are adjusted in time after the quality of water of incoming water fluctuates, the index of the biological system is guaranteed, excess sludge is discharged in time according to the operation of the system and the condition of the sludge, the microbial flora in the sludge is kept in a logarithmic growth period, and higher sludge activity is kept;
step five: the method has the advantages that the wastewater monitoring is enhanced, the wastewater is randomly inspected at irregular intervals, abnormal wastewater is found and reported and adjusted in time, the abnormal wastewater receiving amount is reduced, the received abnormal wastewater is guided into an accident pool in time, the dosage is increased in time at the air flotation source, organic matters are reduced, the water quality entering a biochemical system is stabilized, and the water quality fluctuation impact is avoided;
step six: optimizing indexes, increasing the alkalinity analysis indexes of the aerobic tank, controlling the alkalinity of the aerobic tank at 400mg/l, and controlling the reflux ratio of nitrifying liquid at 3:1, controlling the content of thiocyanide in inlet water of an adjusting tank to be below 1000 mg/l;
obtaining an optimized method for improving biochemical treatment load in wastewater treatment according to the first embodiment;
example two
The method for optimizing and improving the biochemical treatment load in the wastewater treatment is prepared by the following steps:
the method comprises the following steps: increasing the variety of floras to enhance the activity of the floras, adding 440t of high-efficiency biological agent into an aerobic tank of a key core facility, introducing various biological floras and improving the activity of the biological floras, so that the microorganisms can degrade organic matters in the wastewater more efficiently, the nitration reaction rate is improved, the organic matters are removed efficiently in the biological stage, and the adding amount of subsequent chemical agents is reduced;
step two: performing water quality detection operation, performing a flocculation reagent adding test for multiple times according to water quality, and selecting a high-efficiency and economical reagent, wherein the effluent is light in color and the turbidity is stable at 10NTU;
step three: the improved primary air floatation device is utilized to carry out normal use work, and organic matters are reduced from the source;
step four: the sludge reflux flowmeter, the anoxic tank water inlet flowmeter and the excess sludge discharge flowmeter are additionally arranged in a biological treatment stage, so that eyes are added in a biological system, the flow of sludge and the reflux quantity of supernatant of a secondary sedimentation tank are adjusted in time after the quality of water of incoming water fluctuates, the index of the biological system is guaranteed, excess sludge is discharged in time according to the operation of the system and the condition of the sludge, the microbial flora in the sludge is kept in a logarithmic growth period, and higher sludge activity is kept;
step five: the wastewater monitoring is enhanced, the wastewater is randomly inspected, abnormal wastewater is found and reported in time for adjustment, the received abnormal wastewater amount is reduced, the received abnormal wastewater is introduced into an accident pool in time, the dosage is increased in time at the air flotation source, organic matters are reduced, the water quality entering a biochemical system is stabilized, and the fluctuation impact of the water quality is avoided;
step six: optimizing indexes, increasing the alkalinity analysis indexes of the aerobic tank, controlling the alkalinity of the aerobic tank at 500mg/l, and controlling the reflux ratio of nitrifying liquid at 3:1, controlling the content of thiocyanide in inlet water of an adjusting tank to be below 1000 mg/l;
obtaining an optimized method for improving biochemical treatment load in wastewater treatment according to the second embodiment;
EXAMPLE III
The method for optimizing and improving the biochemical treatment load in the wastewater treatment is prepared by the following steps:
the method comprises the following steps: increasing the variety of floras to enhance the activity of the floras, adding 480t of high-efficiency biological agents into an aerobic tank of a key core facility, introducing various biological floras and improving the activity of the biological floras, so that the microorganisms can degrade organic matters in the wastewater more efficiently, the nitration reaction rate is improved, the organic matters are removed efficiently in the biological stage, and the adding amount of subsequent chemical agents is reduced;
step two: performing water quality detection operation, performing a flocculation reagent adding test for multiple times according to water quality, and selecting a high-efficiency and economical reagent, wherein the effluent is light in color and the turbidity is stable at 10NTU;
step three: the improved primary air floatation device is utilized to carry out normal use work, and organic matters are reduced from the source;
step four: the sludge reflux flowmeter, the anoxic tank water inlet flowmeter and the excess sludge discharge flowmeter are additionally arranged in a biological treatment stage, so that eyes are added in a biological system, the flow of sludge and the reflux quantity of supernatant of a secondary sedimentation tank are adjusted in time after the quality of water of incoming water fluctuates, the index of the biological system is guaranteed, excess sludge is discharged in time according to the operation of the system and the condition of the sludge, the microbial flora in the sludge is kept in a logarithmic growth period, and higher sludge activity is kept;
step five: the method has the advantages that the wastewater monitoring is enhanced, the wastewater is randomly inspected at irregular intervals, abnormal wastewater is found and reported and adjusted in time, the abnormal wastewater receiving amount is reduced, the received abnormal wastewater is guided into an accident pool in time, the dosage is increased in time at the air flotation source, organic matters are reduced, the water quality entering a biochemical system is stabilized, and the water quality fluctuation impact is avoided;
step six: optimizing indexes, increasing the alkalinity analysis indexes of the aerobic tank, controlling the alkalinity of the aerobic tank at 600mg/l, and controlling the reflux ratio of nitrifying liquid at 3:1, controlling the content of thiocyanide in inlet water of an adjusting tank to be below 1000 mg/l;
obtaining an optimized method for improving biochemical treatment load in wastewater treatment according to the third embodiment;
further, the primary air flotation device is improved in a mode that two sections of air flotation are transformed into first section air flotation to remove light oil, a perforated aeration pipe is laid at the bottom of the first section of air flotation to continuously aerate and release 2mm of bubbles, and the light oil floats upwards and is scraped to remove slag; the second section adds drugs to carry out coagulation reaction, does not carry out aeration precipitation to carry out slag discharge, and reduces organic matters from the source to the maximum extent;
furthermore, the waste water spot inspection system improves the analysis and report efficiency, can find high-concentration waste water in time, adjusts the system, reduces the possibility that the system receives high-concentration waste water impact, improves the desalting water amount along with biochemical treatment and advanced treatment, optimizes the waste water system balance to the maximum extent, and greatly reduces the environmental protection risk and environmental protection economic penalty of enterprises;
furthermore, the high-efficiency biological agent adopted by the auxiliary additive is a composite biological agent obtained by combining engineering bacteria which are screened from nature and are combined by multiple kinds of bacillus and single pseudomonas and combining an enzyme preparation which is prepared by reasonably proportioning protease, lipase, amylase, urease, cellulase and nitrate reductase, the whole biological agent has a better COD (chemical oxygen demand) removing effect, the flocculating agent adopted by the auxiliary additive is an inorganic high-molecular flocculating agent, the coagulating agent adopted by the auxiliary additive is inorganic high-molecular polyaluminium chloride, the whole cost ratio is higher, the treated water quantity is greatly improved, and the biochemical treated water quantity can be 90m 3 H is increased to 135m 3 H, 45m is increased 3 The continuous discharge of the production wastewater can be ensured;
furthermore, the ammonia nitrogen regulation index of the aerobic tank is increased, the PH value is controlled to be about 8 when the ammonia nitrogen is removed, the PH value is replaced by introducing alkalinity control, the alkalinity is controlled to be 400-600mg/l, the efficient implementation of nitration reaction can be ensured, the water distribution amount of the whole treatment process can be reduced, the quality of biochemical effluent is improved, and the desalted water amount generated by deep treatment is changed from the original 60m 3 Increase of h to 90m 3 And h, the annual benefit can be effectively increased.
Finally, it should be noted that the above-mentioned contents are only used for illustrating the technical solutions of the present invention, and not for limiting the protection scope of the present invention, and those skilled in the art can make simple modifications or equivalent substitutions on the technical solutions of the present invention without departing from the spirit and scope of the technical solutions of the present invention.

Claims (1)

1. A method for optimizing and improving biochemical treatment load in wastewater treatment is characterized by comprising the following steps: the wastewater to be treated is sent into an aerobic tank, biological agents are put into the aerobic tank, an air flotation device is arranged in the aerobic tank, the air flotation device is divided into two sections, the first section is an aeration section, a perforated aeration pipe is laid at the bottom of the aeration pipe, aeration holes with the diameter of 1.8-2.2mm are formed in the aeration pipe, the second section is a dosing section for adding flocculating agents and coagulants, the turbidity is controlled to be stabilized at 9.5-10.5NTU, the aerobic Chi Jiandu is controlled at 400-600mg/L, and the reflux ratio of nitrifying liquid is controlled at 3:1, controlling the content of thiocyanide in inlet water of an adjusting tank to be below 1000 mg/L;
the biological agent is a composite biological agent which is formed by combining engineering bacteria of various bacillus and single pseudomonas screened from the nature and protease, lipase, amylase, urease, cellulase and nitrate reductase;
the flocculant is an inorganic polymeric flocculant;
the coagulant is inorganic high-molecular polyaluminium chloride.
CN202011358307.0A 2020-11-27 2020-11-27 Optimization and improvement method for biochemical treatment load in wastewater treatment Active CN112607960B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202011358307.0A CN112607960B (en) 2020-11-27 2020-11-27 Optimization and improvement method for biochemical treatment load in wastewater treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202011358307.0A CN112607960B (en) 2020-11-27 2020-11-27 Optimization and improvement method for biochemical treatment load in wastewater treatment

Publications (2)

Publication Number Publication Date
CN112607960A CN112607960A (en) 2021-04-06
CN112607960B true CN112607960B (en) 2023-04-18

Family

ID=75227967

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202011358307.0A Active CN112607960B (en) 2020-11-27 2020-11-27 Optimization and improvement method for biochemical treatment load in wastewater treatment

Country Status (1)

Country Link
CN (1) CN112607960B (en)

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1413916A (en) * 2002-07-17 2003-04-30 王文兵 Air-floated biological treatment process and equipment
CN205188076U (en) * 2015-11-26 2016-04-27 河南郑一生生物科技有限公司 Effluent disposal system of cosmetics production
CN107381828B (en) * 2017-04-28 2020-10-23 泰伦特生物工程股份有限公司 Composite microbial preparation for auxiliary treatment of waste cutting fluid and use method
CN108751625B (en) * 2018-08-20 2023-12-29 兴源环境科技股份有限公司 Treatment system and process for fermentation antibiotic wastewater
CN111943447B (en) * 2020-08-21 2022-03-11 诸暨市蓝欣环保科技有限公司 Treatment process of printing and dyeing wastewater

Also Published As

Publication number Publication date
CN112607960A (en) 2021-04-06

Similar Documents

Publication Publication Date Title
CN110040911B (en) Treatment method of copper-containing high-salt printing and dyeing wastewater
CN108996808B (en) Biochemical combined treatment process and equipment for degradation-resistant concentrated water in steel industry
CN210711175U (en) Kitchen garbage anaerobic digestion waste water non-membrane method processing system
CN110818205A (en) System and process for reducing concentration of pollutants in steel comprehensive wastewater
CN112919726A (en) Wastewater treatment process for producing hydrogen peroxide
CN112960861A (en) Biological denitrification treatment process for stainless steel pickling wastewater
CN210885705U (en) Reclaimed water recycling system for petrochemical wastewater
KR101360015B1 (en) Method of reusing treated wastewater and system using the same
CN112209578A (en) Kitchen wastewater treatment system
CN111153564A (en) System and method for treating emulsion wastewater
CN100369835C (en) Treatment process for making sewage as recirculating cooling water
CN112209577A (en) Kitchen wastewater treatment method
CN112607960B (en) Optimization and improvement method for biochemical treatment load in wastewater treatment
CN111606502A (en) Harmless wastewater treatment process and system for livestock and poultry died of diseases
CN111977846A (en) Method for treating high-concentration organophosphorus pesticide wastewater through multistage Fenton catalytic oxidation
CN216236438U (en) Pretreatment system for garbage extrusion leachate
CN211999346U (en) Emulsion wastewater treatment system
CN106745744B (en) Sewage treatment method and sewage treatment system
CN109179874A (en) Fenton oxidation combination constructed wetland plant handles coking wastewater technique
CN215365364U (en) High-toxicity degradation-resistant pesticide wastewater treatment system
CN211445406U (en) Landfill leachate treatment device
CN111762961A (en) Kitchen wastewater treatment method
CN112707584A (en) Method for treating cold-rolling oily wastewater of iron and steel enterprises
CN113526778A (en) Treatment process of high-concentration industrial wastewater
CN220335004U (en) Lithium iron phosphate production wastewater treatment system

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant