CN109354211A - The method for preparing efficient carbon source sewage-treating agent needed for denitrifying microorganism with by-product sodium acetate - Google Patents

The method for preparing efficient carbon source sewage-treating agent needed for denitrifying microorganism with by-product sodium acetate Download PDF

Info

Publication number
CN109354211A
CN109354211A CN201811266499.5A CN201811266499A CN109354211A CN 109354211 A CN109354211 A CN 109354211A CN 201811266499 A CN201811266499 A CN 201811266499A CN 109354211 A CN109354211 A CN 109354211A
Authority
CN
China
Prior art keywords
sodium acetate
carbon source
treating agent
kettle
source sewage
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
Application number
CN201811266499.5A
Other languages
Chinese (zh)
Inventor
沈晓峰
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.)
Shoujian Technology Co.,Ltd.
Original Assignee
Qiaochang Modern Agriculture 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 Qiaochang Modern Agriculture Co Ltd filed Critical Qiaochang Modern Agriculture Co Ltd
Priority to CN201811266499.5A priority Critical patent/CN109354211A/en
Publication of CN109354211A publication Critical patent/CN109354211A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/34Biological treatment of water, waste water, or sewage characterised by the microorganisms used
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/28Anaerobic digestion processes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/30Aerobic and anaerobic processes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/34Biological treatment of water, waste water, or sewage characterised by the microorganisms used
    • C02F3/348Biological treatment of water, waste water, or sewage characterised by the microorganisms used characterised by the way or the form in which the microorganisms are added or dosed
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2305/00Use of specific compounds during water treatment
    • C02F2305/06Nutrients for stimulating the growth of microorganisms

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Microbiology (AREA)
  • Biodiversity & Conservation Biology (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)

Abstract

The invention discloses a kind of methods for preparing efficient carbon source sewage-treating agent needed for denitrifying microorganism with by-product sodium acetate, including extracting the device of sodium acetate from waste water and configuring high efficiency composition carbon source sewage-treating agent by primary raw material of sodium acetate;Waste water is sequentially connected through the pipeline with pump to be neutralized kettle, takes off light kettle, adsorption tower, is concentrated by evaporation kettle, cooler, crystallization kettle, centrifuge and mother liquor storage tank are connected by pipeline, sodium acetate is obtained to crystallize into batch mixer, it is packed with after glucose, phosphorus nutritional agent mixed configuration, as high efficiency composition carbon source sewage-treating agent.Compared with prior art, the invention has the following advantages that the present invention recycles the sodium acetate that chemical engineering industry production process generates, and using sodium acetate as primary raw material, prepare efficient carbon source sewage-treating agent needed for denitrifying microorganism, resource utilization sodium acetate, recycling preparation facilities small investment of the invention, preparation process are simple, the efficient carbon source sewage-treating agent use process of preparation is simple, reduces the technical difficulty of charging.

Description

Efficient carbon source sewage-treating agent needed for denitrifying microorganism is prepared with by-product sodium acetate Method
Technical field
The present invention relates to field of waste water treatment additional carbon technical fields, more particularly to use by-product sodium acetate system The method of efficient carbon source sewage-treating agent needed for standby denitrifying microorganism.
Background technique
Acetic acid is a kind of important industrial chemicals, is widely used in the industrial circles such as chemical industry, light textile, medicine, dyestuff.Changing In work industrial processes, acid binding agent or pH value adjustment agent frequently as reaction, the acetic acid for consuming or generating in industrial production, Often entered in waste water in the form of acetate or acetic acid, such COD value of waste water is high, when handling using biochemical method, occupies industry Biochemical treatment of wastewater load, while a large amount of sludge are generated, acetic acid is also not used, and results in waste of resources.
Meanwhile during sanitary sewage disposal, organic nitrogen, proteinic nitrogen in sewage etc. are first under aerobic or oxygen free condition It is first oxidized or hydrolysis is ammonia nitrogen, be then oxidized to nitrate nitrogen under the action of aerobic autotrophic nitrifier.Then lacking It under the conditions of oxygen, is acted on by denitrifying bacterium, and there is offer electronics and proton, nitrate nitrogen by carbon source to make nitre state as electron acceptor Nitrogen is reduced into nitrogen and escapes from sewage, achievees the purpose that removing total nitrogen.During nitrification and denitrification, its nitric efficiency is influenced Key factor be denitrifying carbon source concentration.In biological denitrification system, nitrifier will have sufficient carbon source as electron donor, It can promote going on smoothly for denitrification.
It is low and be unable to satisfy normal life to be generally faced with raw sewage carbon-nitrogen ratio for major part urban wastewater treatment firm in China's at present The problem of object denitrogenation dephosphorizing carbon source demand.Therefore, most of urban wastewater treatment firm is needed by throwing into sewage disposal system Add a certain amount of additional carbon to improve system denitrogenation dephosphorizing efficiency.
Denitrifying bacterium is the facultative oxygen-starved microorganism of a kind of chemoheterotrophy, and reaction need to carry out under conditions of anoxic, instead Denitrifying bacterium during answering is carried out anoxic and is exhaled using various organic matters as electron donor using nitrate as electron acceptor It inhales.In the biochemical treatment denitrification process section of waste water, denitrifying bacterium living environment must assure that suitable carbon-nitrogen ratio and and Phosphorus nutritional agent.
In addition, different types of additional carbon influences difference to the denitrification process of system, even if adding same amount of outer Adding carbon source, the effect of processing is also not quite similar, and the additional carbon of some types can quickly respond after adding, and some The carbon source of type then needs just play a role after one section of adaptation time and domestication, there is certain hysteresis quality, cannot be perfect It optimizes the system operation on ground.
Currently, commercially available additional carbon, carbon source single variety, such as sodium acetate, methanol, sucrose or glucose, however it is anti- Nitrifying bacteria community is the combination of the microorganism in different stages of growth of mixing, and the carbon source supplement of single variety is not able to satisfy each The nutritional need of a stage microorganism, requires supplementation with several kinds of carbon source and phosphorus nutritional agent, and it is different that when supplement needs professional to match Carbon source and phosphorus nutritional agent, operating process are complicated.
Therefore, how to provide one kind has the characteristics that energy saving, protection environment, operating process is simple, carbon source is wide in variety The method for preparing efficient carbon source sewage-treating agent needed for denitrifying microorganism with by-product sodium acetate be those skilled in the art urgently Problem to be solved.
Summary of the invention
In view of this, having the present invention provides one kind, energy saving, protection environment, operating process be simple, carbon source kind The method for preparing efficient carbon source sewage-treating agent needed for denitrifying microorganism with by-product sodium acetate of the features such as more.
To achieve the above object, the invention provides the following technical scheme:
The method for preparing efficient carbon source sewage-treating agent needed for denitrifying microorganism with by-product sodium acetate characterized by comprising The device of sodium acetate is extracted from waste water and configures high efficiency composition carbon source sewage-treating agent by primary raw material of sodium acetate;The dress It sets including neutralizing kettle, taking off light kettle, adsorption tower, sorbent regeneration system, crystallization kettle, centrifuge and batch mixer;The waste water is through band The pipeline of pump be sequentially connected neutralize kettle, take off light kettle, adsorption tower, be concentrated by evaporation kettle, by pipeline connect cooler, crystallization kettle, from Scheming and mother liquor storage tank obtain sodium acetate and crystallize into batch mixer, and pack after glucose, phosphorus nutritional agent mixed configuration, as efficiently Compounded carbons sewage-treating agent;Wherein, required raw material comprises the following raw materials by weight percent: 50~99% acetate trihydrate Sodium, 1~50% cerelose, 0~1% phosphorus nutritional agent;The phosphorus nutritional agent is one of phosphate or a variety of;It is described Phosphate is sodium phosphate, potassium phosphate, sodium dihydrogen phosphate, potassium dihydrogen phosphate or tertiary sodium phosphate, preferably tertiary sodium phosphate.
Preferably, a kind of efficient carbon source sewage-treating agent needed for denitrifying microorganism is prepared with by-product sodium acetate above-mentioned In method, process flow are as follows: waste water containing sodium acetate → neutralization → vacuum removal light component → filtering → adsorption bleaching removal of impurities → Evaporation and concentration → crystallization → drying → mixture → packaging.
Preferably, a kind of efficient carbon source sewage-treating agent needed for denitrifying microorganism is prepared with by-product sodium acetate above-mentioned In method, comprising the following steps:
A) waste water containing sodium acetate for generating chemical engineering industry production process is put into neutralizing tank, and adding sodium hydroxide is neutralized, and is adjusted Save pH to 6.5 ~ 7;
B) above-mentioned neutralizer is squeezed into vacuum to take off in light kettle, removes the light component contained in filtrate, cool down 40 DEG C hereinafter, through pocket type Filter is filtered to remove impurity;
C) by filtered solution, the adsorption tower of macroreticular resin is housed, removes the color and other organic impurities of solution, macropore Resin is through resolution system regenerated from washing;
D) decoloration is removed into mixture solution and is concentrated into relative density 1.20~1.30 through evaporator, squeezed into crystallization kettle and crystallized, crystallized It after 10 hours, dries and separates through centrifuge, obtain Sodium acetate trihydrate, mother liquor returns neutralization kettle and applies;
E) Sodium acetate trihydrate is pressed into following weight percent, mixed configuration is high efficiency composition carbon source sewage-treating agent, weight percent The raw material of ratio forms: Sodium acetate trihydrate 50~99%, other carbon sources 1~50%, phosphorus nourishing agent 0~1%, mixed configuration is efficient Compounded carbons sewage-treating agent.
Preferably, a kind of efficient carbon source sewage-treating agent needed for denitrifying microorganism is prepared with by-product sodium acetate above-mentioned In method, adsorption bleaching removal of impurities can be adsorbed with powder electroless plating or macroporous absorbent resin in the step b), preferred macropore Adsorb resin.
Preferably, a kind of efficient carbon source sewage-treating agent needed for denitrifying microorganism is prepared with by-product sodium acetate above-mentioned In method, one of described other carbon sources in addition to sodium acetate or a variety of.
Preferably, a kind of efficient carbon source sewage-treating agent needed for denitrifying microorganism is prepared with by-product sodium acetate above-mentioned In method, other carbon sources are cerelose, industrial sucrose, citric acid etc., preferably cerelose.
Preferably, a kind of efficient carbon source sewage-treating agent needed for denitrifying microorganism is prepared with by-product sodium acetate above-mentioned In method, macroporous absorbent resin described in the step c) is styrene tyle macroporous adsorption resin.
It can be seen via above technical scheme that compared with prior art, the invention has the following advantages that
The sodium acetate that chemical engineering industry production process generates is recycled, and using sodium acetate as primary raw material, prepares the micro- life of denitrification It is prepared by efficient carbon source sewage-treating agent needed for object, resource utilization sodium acetate, recycling preparation facilities small investment of the invention Journey is simple, and the efficient carbon source sewage-treating agent use process of preparation is simple, reduces the technical difficulty of charging.
Specific embodiment
Below in conjunction with the embodiment of the present invention, technical scheme in the embodiment of the invention is clearly and completely described, Obviously, described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.Based in the present invention Embodiment, every other embodiment obtained by those of ordinary skill in the art without making creative efforts, all Belong to the scope of protection of the invention.
The embodiment of the invention discloses one kind to have energy saving, protection environment, operating process is simple, carbon source is wide in variety etc. The method for preparing efficient carbon source sewage-treating agent needed for denitrifying microorganism with by-product sodium acetate of feature.
Please refer to disclosed by the invention a kind of prepared at efficient carbon source sewage needed for denitrifying microorganism with by-product sodium acetate The method for managing agent, specifically includes:
The device of sodium acetate is extracted from waste water and configures high efficiency composition carbon source sewage-treating agent by primary raw material of sodium acetate;Institute Stating device includes neutralizing kettle, taking off light kettle, adsorption tower, sorbent regeneration system, crystallization kettle, centrifuge and batch mixer;The waste water It is sequentially connected through the pipeline with pump and neutralizes kettle, take off light kettle, adsorption tower, be concentrated by evaporation kettle, cooler, crystallization are connected by pipeline Kettle, centrifuge and mother liquor storage tank obtain sodium acetate and crystallize into batch mixer, and pack after glucose, phosphorus nutritional agent mixed configuration, as High efficiency composition carbon source sewage-treating agent;Wherein, required raw material comprises the following raw materials by weight percent: 50~99% three water Sodium acetate, 1~50% cerelose, 0~1% phosphorus nutritional agent;The phosphorus nutritional agent is one of phosphate or a variety of; The phosphate is sodium phosphate, potassium phosphate, sodium dihydrogen phosphate, potassium dihydrogen phosphate or tertiary sodium phosphate, preferably tertiary sodium phosphate.
The present invention in view of the above technology the problem of, recycle chemical engineering industry production process generate acetic acid or vinegar Sour sodium prepares a kind of high efficiency composition carbon source sewage-treating agent containing compounded carbons and phosphorus nutritional agent, need to only supplement a kind of processing Agent reduces the technical difficulty of charging;In order to solve the deficiency of the above technology, the present invention provides extract from chemical production wastewater Sodium acetate simultaneously prepares a kind of high efficiency composition carbon source sewage-treating agent containing compounded carbons and phosphorus nutritional agent, will be useless containing sodium acetate Water is neutralized, adsorption bleaching removal of impurities, is concentrated by evaporation, crystallization, obtains sodium acetate, prepares one kind as primary raw material using this sodium acetate and contain There are the high efficiency composition carbon source sewage-treating agent of compounded carbons and phosphorus nutritional agent, resource utilization sodium acetate.
In order to further optimize the above technical scheme, process flow are as follows: waste water containing sodium acetate → neutralization → vacuum removal Light component → filtering → adsorption bleaching removal of impurities → evaporation and concentration → crystallization → drying → mixture → packaging.
In order to further optimize the above technical scheme, comprising the following steps:
A) waste water containing sodium acetate for generating chemical engineering industry production process is put into neutralizing tank, and adding sodium hydroxide is neutralized, and is adjusted Save pH to 6.5 ~ 7;
B) above-mentioned neutralizer is squeezed into vacuum to take off in light kettle, removes the light component contained in filtrate, cool down 40 DEG C hereinafter, through pocket type Filter is filtered to remove impurity;
C) by filtered solution, the adsorption tower of macroreticular resin is housed, removes the color and other organic impurities of solution, macropore Resin is through resolution system regenerated from washing;
D) decoloration is removed into mixture solution and is concentrated into relative density 1.20~1.30 through evaporator, squeezed into crystallization kettle and crystallized, crystallized It after 10 hours, dries and separates through centrifuge, obtain Sodium acetate trihydrate, mother liquor returns neutralization kettle and applies;
E) Sodium acetate trihydrate is pressed into following weight percent, mixed configuration is high efficiency composition carbon source sewage-treating agent, weight percent The raw material of ratio forms: Sodium acetate trihydrate 50~99%, other carbon sources 1~50%, phosphorus nourishing agent 0~1%, mixed configuration is efficient Compounded carbons sewage-treating agent.
In order to further optimize the above technical scheme, adsorption bleaching removal of impurities can use powder electroless plating or big in step b) Macroporous adsorbent resin absorption, preferred macroporous absorbent resin.
In order to further optimize the above technical scheme, compounded carbons are one of other carbon sources in addition to sodium acetate or more Kind;Other carbon sources are cerelose, industrial sucrose, citric acid etc., preferably cerelose.
In order to further optimize the above technical scheme, phosphorus nutritional agent is one of phosphate or a variety of;Phosphate is phosphorus Sour sodium, potassium phosphate, sodium dihydrogen phosphate, potassium dihydrogen phosphate, tertiary sodium phosphate etc.., preferred tertiary sodium phosphate.
In order to further optimize the above technical scheme, macroporous absorbent resin described in step c is styrene tyle macroporous absorption tree Rouge;The solution after taking off gently is passed through macropore with certain flow velocity and inhaled wet method dress post application in the form of round resin column bed Attached resin, the solution pass through resin column bed with the flow velocity of 0.5~2.0 times of resin total volume per hour, preferably per hour 0.8~ The flow velocity of 1.2 times of resin total volumes passes through resin column bed;The height of round resin column bed and diameter ratio (i.e. ratio of height to diameter) be 2 or It is bigger, preferably greater than or equal to 4.
In order to further optimize the above technical scheme, substance that show color and impurity in the adsorbance of macroporous absorbent resin and solution Concentration and resin characteristic it is related, in a particular embodiment using column bed lower end outlet color change as foundation, color is by colourless Stop charging when thin out yellow, treating capacity is 1-15000 times of resin total volume.
In order to further optimize the above technical scheme, in the step c, the substance that show color in the solution is attracted to tree On rouge, using parsing agent to the substance that show color being adsorbed on resin into parsing, parsing agent used can be methanol or ethanol solution, It is preferred that methanol;The flow velocity for parsing agent be per hour be 0.5~1.0 times of resin total volume, preferred 0.75 times of resin totality per hour Product;Strippant dosage is 0.5-20 times of styrene tyle macroporous adsorption resin admission space;After the regeneration of organic solvent regenerative agent It can put back into, the parsing agent containing colour developing organic matter, can be used repeatedly as parsing agent after rectifying column rectifying.
In order to further optimize the above technical scheme, specific embodiment are as follows: clethodim intermediate 6- second sulfydryl-heptane -3 Alkene -2- ketone production process, in the washing water of generation containing 15% sodium acetate, 5% methanol, color is fallow.From washing water The middle method extracted sodium acetate and prepare efficient carbon source sewage-treating agent, it is characterised in that the following steps are included:
A) sodium acetate washing water will be contained to be put into neutralizing tank, adding sodium hydroxide is neutralized, and pH to 6.5 ~ 7 is adjusted;
B) above-mentioned neutralizer is squeezed into vacuum to take off in light kettle, removes the light component contained in filtrate, cool down 40 DEG C hereinafter, through pocket type Filter is filtered to remove impurity;
C) by filtered solution, the adsorption tower of macroreticular resin is housed, removes the color and other organic impurities of solution, macropore Resin is through resolution system regenerated from washing;
D) decoloration is removed into mixture solution and is concentrated into relative density 1.20~1.30 through evaporator, squeezed into crystallization kettle and crystallized, crystallized It after 10 hours, dries and separates through centrifuge, obtain Sodium acetate trihydrate, mother liquor returns neutralization kettle and applies.
E) by Sodium acetate trihydrate, cerelose, tertiary sodium phosphate, by Sodium acetate trihydrate 90%, cerelose 9%, phosphoric acid 1% weight percent of trisodium is sequentially added and is stirred in mixing machine 30 minutes, and mixed configuration is at high efficiency composition carbon source sewage Manage agent.
In order to further optimize the above technical scheme, specific embodiment: Binzhou sewage treatment plant (ordinary municipal sewage Factory), biochemical treatment of wastewater influent COD cr is 250mg/L or so, ammonia nitrogen 36mg/L, PH6.4, and processing water is respectively 20000 ton/days.Since ammonia nitrogen value is higher, removal rate can be improved by adding suitable carbon source;
Contrast groups: 99% cerelose;
Experimental group: the high efficiency composition carbon source sewage-treating agent that embodiment 1 configures;
Configure control group glucose and experimental group high efficiency composition carbon source sewage-treating agent to water respectively 15% solution (weight Percentage);
The control group nutrient solution that adds of sewage disposal system is 2000 kg/days, and by operation in 15 days, total nitrogen removal effect was not Good, water outlet COD is 80mg/L or so, and total nitrogen is 17mg/L or so.Use experimental group nutrient solution instead, dosage is still 2000 kilograms/ It, the experimental group water outlet COD by operations in 15 days is 40mg/L or so, and total nitrogen is 5mg/L or so;
The ammonia nitrogen removal of contrast groups is ineffective, and the general CODcr that is discharged is 50mg/L or so, and ammonia nitrogen is 6~7mg/L;And it tests It is 40mg/L or so that group has just reached water outlet CODcr after using 1 day, and ammonia nitrogen is 2~3mg/L, and significant effect improves.
Each embodiment in this specification is described in a progressive manner, the highlights of each of the examples are with other The difference of embodiment, the same or similar parts in each embodiment may refer to each other.For device disclosed in embodiment For, since it is corresponded to the methods disclosed in the examples, so being described relatively simple, related place is said referring to method part It is bright.
The foregoing description of the disclosed embodiments enables those skilled in the art to implement or use the present invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, as defined herein General Principle can be realized in other embodiments without departing from the spirit or scope of the present invention.Therefore, of the invention It is not intended to be limited to the embodiments shown herein, and is to fit to and the principles and novel features disclosed herein phase one The widest scope of cause.

Claims (7)

1. the method for preparing efficient carbon source sewage-treating agent needed for denitrifying microorganism with by-product sodium acetate, which is characterized in that packet It includes: extracting the device of sodium acetate from waste water and configure high efficiency composition carbon source sewage-treating agent by primary raw material of sodium acetate;Institute Stating device includes neutralizing kettle, taking off light kettle, adsorption tower, sorbent regeneration system, crystallization kettle, centrifuge and batch mixer;The waste water It is sequentially connected through the pipeline with pump and neutralizes kettle, take off light kettle, adsorption tower, be concentrated by evaporation kettle, cooler, crystallization are connected by pipeline Kettle, centrifuge and mother liquor storage tank obtain sodium acetate and crystallize into batch mixer, and pack after glucose, phosphorus nutritional agent mixed configuration, as High efficiency composition carbon source sewage-treating agent;Wherein, required raw material comprises the following raw materials by weight percent: 50~99% three water Sodium acetate, 1~50% cerelose, 0~1% phosphorus nutritional agent;The phosphorus nutritional agent is one of phosphate or a variety of; The phosphate is sodium phosphate, potassium phosphate, sodium dihydrogen phosphate, potassium dihydrogen phosphate or tertiary sodium phosphate, preferably tertiary sodium phosphate.
2. according to claim 1 prepare efficient carbon source sewage-treating agent needed for denitrifying microorganism with by-product sodium acetate Method, which is characterized in that its process flow are as follows: waste water containing sodium acetate → neutralization → vacuum removal light component → filtering → absorption is de- Color removal of impurities → evaporation and concentration → crystallization → drying → mixture → packaging.
3. according to claim 2 prepare efficient carbon source sewage-treating agent needed for denitrifying microorganism with by-product sodium acetate Method, which comprises the following steps:
A) waste water containing sodium acetate for generating chemical engineering industry production process is put into neutralizing tank, and adding sodium hydroxide is neutralized, and is adjusted Save pH to 6.5 ~ 7;
B) above-mentioned neutralizer is squeezed into vacuum to take off in light kettle, removes the light component contained in filtrate, cool down 40 DEG C hereinafter, through pocket type Filter is filtered to remove impurity;
C) by filtered solution, the adsorption tower of macroreticular resin is housed, removes the color and other organic impurities of solution, macropore Resin is through resolution system regenerated from washing;
D) decoloration is removed into mixture solution and is concentrated into relative density 1.20~1.30 through evaporator, squeezed into crystallization kettle and crystallized, crystallized It after 10 hours, dries and separates through centrifuge, obtain Sodium acetate trihydrate, mother liquor returns neutralization kettle and applies;
E) Sodium acetate trihydrate is pressed into following weight percent, mixed configuration is high efficiency composition carbon source sewage-treating agent, weight percent The raw material of ratio forms: Sodium acetate trihydrate 50~99%, other carbon sources 1~50%, phosphorus nourishing agent 0~1%, mixed configuration is efficient Compounded carbons sewage-treating agent.
4. according to claim 3 prepare efficient carbon source sewage-treating agent needed for denitrifying microorganism with by-product sodium acetate Method, which is characterized in that adsorption bleaching removal of impurities can be adsorbed with powder electroless plating or macroporous absorbent resin in the step b), Preferred macroporous absorbent resin.
5. according to claim 1 prepare efficient carbon source sewage-treating agent needed for denitrifying microorganism with by-product sodium acetate Method, which is characterized in that one of described other carbon sources in addition to sodium acetate are a variety of.
6. according to claim 5 prepare efficient carbon source sewage-treating agent needed for denitrifying microorganism with by-product sodium acetate Method, which is characterized in that other carbon sources are cerelose, industrial sucrose, citric acid etc., preferably cerelose.
7. according to claim 3 prepare efficient carbon source sewage-treating agent needed for denitrifying microorganism with by-product sodium acetate Method, which is characterized in that macroporous absorbent resin described in the step c) is styrene tyle macroporous adsorption resin.
CN201811266499.5A 2018-10-29 2018-10-29 The method for preparing efficient carbon source sewage-treating agent needed for denitrifying microorganism with by-product sodium acetate Pending CN109354211A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811266499.5A CN109354211A (en) 2018-10-29 2018-10-29 The method for preparing efficient carbon source sewage-treating agent needed for denitrifying microorganism with by-product sodium acetate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811266499.5A CN109354211A (en) 2018-10-29 2018-10-29 The method for preparing efficient carbon source sewage-treating agent needed for denitrifying microorganism with by-product sodium acetate

Publications (1)

Publication Number Publication Date
CN109354211A true CN109354211A (en) 2019-02-19

Family

ID=65346937

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811266499.5A Pending CN109354211A (en) 2018-10-29 2018-10-29 The method for preparing efficient carbon source sewage-treating agent needed for denitrifying microorganism with by-product sodium acetate

Country Status (1)

Country Link
CN (1) CN109354211A (en)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5352825A (en) * 1993-07-06 1994-10-04 Hoarmann & Reimer Corp. Recovery of organic acid salts from impure process streams by addition of bases
CN102583853A (en) * 2012-01-05 2012-07-18 浙江金科过氧化物股份有限公司 Combined treatment method for two kinds of waste acid water generated in tetraacetylethylenediamine (TAED) production
CN103043843A (en) * 2012-12-28 2013-04-17 山东金缘生物科技有限公司 Device and method for extracting sodium acetate from tower bottom wastewater of primary tower in furfural production
CN103865796A (en) * 2014-03-21 2014-06-18 杭州水询环保科技有限公司 Microbial complex nutrient solution for biological treatment of wastewater
CN106800506A (en) * 2016-12-30 2017-06-06 杭州垚信生物科技有限公司 A kind of preparation method of anhydrous sodium acetate
CN107602373A (en) * 2017-09-13 2018-01-19 山西恒德益生物科技有限公司 A kind of method that sodium acetate is extracted from furfural production waste water

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5352825A (en) * 1993-07-06 1994-10-04 Hoarmann & Reimer Corp. Recovery of organic acid salts from impure process streams by addition of bases
CN102583853A (en) * 2012-01-05 2012-07-18 浙江金科过氧化物股份有限公司 Combined treatment method for two kinds of waste acid water generated in tetraacetylethylenediamine (TAED) production
CN103043843A (en) * 2012-12-28 2013-04-17 山东金缘生物科技有限公司 Device and method for extracting sodium acetate from tower bottom wastewater of primary tower in furfural production
CN103865796A (en) * 2014-03-21 2014-06-18 杭州水询环保科技有限公司 Microbial complex nutrient solution for biological treatment of wastewater
CN106800506A (en) * 2016-12-30 2017-06-06 杭州垚信生物科技有限公司 A kind of preparation method of anhydrous sodium acetate
CN107602373A (en) * 2017-09-13 2018-01-19 山西恒德益生物科技有限公司 A kind of method that sodium acetate is extracted from furfural production waste water

Similar Documents

Publication Publication Date Title
CN102515364B (en) Broad-spectrum bio-energizer for industrial wastewater treatment and preparation method thereof
CN106242045B (en) A kind of aerobic particle mud fast culture process
US20210363039A1 (en) Preparation Method and Application of External Carbon Source by Denitrification from Lake Algae
WO2015089971A1 (en) Natural pyrrhotite biological filter and method for utilizing same to synchronously remove nitrate-nitrogen and phosphorus from water
CN104176824B (en) A kind of ammonium nitrate wastewater biochemical treatment apparatus and operation method
CN108101228A (en) A kind of wastewater treatment microbial microbial inoculum
CN105016470B (en) Method for realizing advanced nitrogen and phosphorus removal of low C/N and C/P municipal sewage through excess sludge anaerobic fermentation mixture
CN104671613B (en) A kind for the treatment of process of percolate from garbage filling field
JPH08500320A (en) Method for processing nitrogen-rich liquid organic waste, fertilizer solution obtained thereby, and use thereof
CN112456643A (en) System and method for realizing partial anaerobic ammonia oxidation deep nitrogen and phosphorus removal by circulating and alternately utilizing main flow and side flow zone biomembrane of urban sewage treatment plant
CN102190371A (en) Breeding method for anaerobic ammonium oxidation granular sludge
CN115057534B (en) Low-carbon sewage nitrogen and phosphorus removal system and process
CN204417293U (en) A kind of denitrification dephosphorization apparatus
CN111517481A (en) Composite carbon source for deep denitrification of leather wastewater and preparation method thereof
CN107473546A (en) A kind of special repair materials of mercury and its preparation technology
CN115043486A (en) Method for deep denitrification by using modified zeolite
CN115140842A (en) Process and device for synchronously removing nitrogen and phosphorus from sewage by using denitrification
CN113698052A (en) Municipal sludge organic matter concentration recycling process
CN105565618A (en) High-efficiency sewage treatment method by denitrification and dephosphorization
CN116495889B (en) Constructed wetland treatment system and treatment method for enhanced denitrification
CN109721163A (en) The method for handling the waste water containing nitrate ion
CN108083452A (en) A kind of heterotrophism integrates solid phase denilrification system with sulphur autotrophy and handles high nitric acid body of salt
CN109354211A (en) The method for preparing efficient carbon source sewage-treating agent needed for denitrifying microorganism with by-product sodium acetate
CN113648991B (en) Deamination catalyst capable of stably producing nitrous nitrogen, preparation method and application thereof
CN110342729A (en) A kind of livestock breeding wastewater integration dephosphorization equipment and its treatment process

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
TA01 Transfer of patent application right

Effective date of registration: 20201223

Address after: 256600 south side of xinyongxin Road, Binbei office, Bincheng District, Binzhou City, Shandong Province

Applicant after: Shoujian Technology Co.,Ltd.

Address before: 256600 southeast of Qinhuangtai and south of Yongxi Road, Binzhou City, Shandong Province

Applicant before: QIAOCHANG MODERN AGRICULTURE Co.,Ltd.

TA01 Transfer of patent application right