CN1887737A - Fast culture process in anaerobic grain sludge - Google Patents

Fast culture process in anaerobic grain sludge Download PDF

Info

Publication number
CN1887737A
CN1887737A CNA2006100129516A CN200610012951A CN1887737A CN 1887737 A CN1887737 A CN 1887737A CN A2006100129516 A CNA2006100129516 A CN A2006100129516A CN 200610012951 A CN200610012951 A CN 200610012951A CN 1887737 A CN1887737 A CN 1887737A
Authority
CN
China
Prior art keywords
reactor
sludge
polyquaternium
anaerobic
olr
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
CNA2006100129516A
Other languages
Chinese (zh)
Inventor
岳秀萍
李亚新
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.)
Taiyuan University of Technology
Original Assignee
Taiyuan University of Technology
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 Taiyuan University of Technology filed Critical Taiyuan University of Technology
Priority to CNA2006100129516A priority Critical patent/CN1887737A/en
Publication of CN1887737A publication Critical patent/CN1887737A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Landscapes

  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

The fast culture process of anaerobic granular sludge belongs to the field of bitanical waste water treating technology, and features that polyquaternary ammonium salt is thrown to reinforce the immobilization of anaerobes to form granular sludge fast. Throwing polyquaternary ammonium salt can reserve methane sarcina to speed the accumulation of methane sarcina, raise the methane producing activity of biological grain and shorten the granulating process. The present invention makes it possible to shorten the starting time of anaerobic reactor to 1-3 months. The polyquaternary ammonium salt as flocculant hard to biodegrade may be absorbed by microbes to form granular sludge with high active component content. The positively charged polyquaternary ammonium salt may be absorbed and adsorbed by negatively charged bacteria to create great amount of biological aggregate capable of strengthening the biological floc, so as to form compact granular sludge with excellent depositing performance.

Description

A kind of fast culture process of anaerobic grain sludge
Technical field
The fast culture process of a kind of anaerobic grain sludge of the present invention belongs to the biological wastewater treatment technology field.Specifically, be to adopt to add polyquaternium and come the technology of reinforced anaerobic microorganism self immobilization with quick formation granule sludge.
Technical background
The anaerobic waste water biologic treating technique is with less energy consumption, and surplus sludge volume is few, emission-free pollution, and reactor organic loading height, volume is little, can reduce special advantages such as initial cost and be subjected to extensive concern.New and effective anaerobic reactor all is to be principal character to form granule sludge.
Dispergated digested sludge is inoculated in the newly-built anaerobic reactor, make reactor progressively bring up to design loading from initial organic loading rate Orgenic Loading Rate-OLR, and in reactor, turn out the active height of capacity, the anaerobic grain sludge that settling property is good, this process is called the startup of reactor.Because the generation time of anaerobion is long, lower than rate of rise, mud increasess slowly, so anaerobic reactor is generally longer start time, needs 4~6 months at least, even more than 1 year.In actual engineering, toggle speed becomes the bottleneck of restriction high efficiency anaerobic reactor widespread use slowly.
Flocculation agent has strengthening effect to promote disperseing mud to form particle, but the dosing method of currently used flocculation agent kind and flocculation agent, to add dosage all uncertain, and the randomness of action effect is very big, uses to engineering and brings blindness and uncertainty; Also there is not at present to adopt the technology that polyquaternium promotes the mud quick particleization that adds.
The type of anaerobic grain sludge mainly contains two kinds: based on the A-type particle mud of sarcina methanica (Methanosarcina) with based on the B type particles mud of methanothrix sp.When formation was the A-type particle mud of dominant bacteria with the sarcina methanica in the reactor, it loaded high, and degradation of substrates speed is fast; And methanothrix sp can only utilize the acetate growth, and cell proliferation is slow, utilizes substrate reactions speed low.But, because sarcina methanica light specific gravity, particle diameter are little, run off with water outlet easily, in anaerobic reactor, be difficult for forming A-type particle mud, this is that the limited reactions device produces the internal cause that methane speed improves.In anaerobic reactor, cultivate selectively and develop sarcina methanica, and formation A-type particle mud, can in the anaerobic reactor of handling high concentrated organic wastewater, accelerate the conversion rate of acetate to methane, acidification rate has following significance greater than the root problem of methanation speed in the solution process operation:
The organic loading rate sarcina methanica of raising system is strong to the acetate metabolism ability, when acetic acid concentration during greater than 300mg/L, is 3~5 times of methanothrix sp to the speed of utilizing of acetate.Therefore A-type particle mud can be brought into play the high and physio-biochemical characteristics faster than rate of growth of substrate utilization speed under its high acetic acid concentration to greatest extent, shortens hydraulic detention time HRT, improves the organic loading rate OLR of system.
The reaction process sarcina methanica of hydrogen transference between quickening to plant, promotion anaerobic digester system is to utilize acetate, H 2/ CO 2Have a liking for hydrogen, have a liking for the acetic acid and methane producing bacterium, can reduce the hydrogen dividing potential drop in the growing environment, for the growth of producing the hydrogen acetogen creates conditions, quicken hydrogen transference between the kind in the anaerobic digestion process, finish organism fast and effectively to CH 4+ CO 2Conversion process.
The basicity demand is little, reduces the running cost sarcina methanica and can adapt to than the lower pH condition of the desired pH value of other methanogen scope, and its anti-acetate energy force rate methanothrix sp is big, can grow under high acetic acid concentration, can reduce the basicity dosage.
Summary of the invention
The purpose of the fast culture process of a kind of anaerobic grain sludge of the present invention is: proposing to form with the sarcina methanica in the anaerobic reactor is the process strategies of the granule sludge of dominant bacteria, thereby discloses the technology that a kind of polyquaternium reinforced anaerobic reactor starts fast.
The fast culture process of a kind of anaerobic grain sludge of the present invention; it is characterized in that it being that a kind of quick formation is the cultural method of the anaerobic grain sludge of dominant bacteria with the sarcina methanica; concrete processing method is: be granular sludge promotor with the polyquaternium; control OLR with chemical oxygen demand (COD) Chemical Oxygen Demand-COD clearance between the starting period; Fe, Co, Ni salt compounds are directly added in the reactor
Raw material:
Seed sludge: municipal sewage plant's digested sludge;
Substratum: with carbohydrate organic waste water is substratum;
Granular sludge promotor: polyquaternium;
Salt compounds: FeCl 2, CoCl 2And NiCl 2
Condition:
I, the stirring of employing strength, mechanical stirring or waterpower alr mode;
II, employing dosing method at interval add polyquaternium in anaerobic reactor;
III, initial OLR adopt 0.5gCOD/ (Ld), are the timed interval that prerequisite determines to improve OLR with COD clearance ≮ 85%;
IV, directly add to Fe, Co, Ni salt compounds in the reactor;
V, height for reactor and diameter ratio H/D get 5~6 and are advisable.
The fast culture process advantage and the purposes of a kind of anaerobic grain sludge of the present invention:
Mud increasess slowly in I, the anaerobic reactor, and initial start stage mud runs off easily.Sarcina methanica light specific gravity, particle diameter are little, suspend easily and run off with water outlet.Add polyquaternium and be not only the effective technology measure that keeps sarcina methanica, accelerates the sarcina methanica accumulation; and for the methanogenesis activity that improves biological particles, shorten the granulating process and also brought into play active effect, start time of anaerobic reactor is shortened 1~3 month.
II, polyquaternium are the flocculation agents of difficult anaerobic biodegradation, can be absorbed activeconstituents height in the formed granule sludge by microorganism gradually after starting end.
III, because polyquaternium has positive charge, and the antibiont capacity of decomposition is strong, can create a large amount of bio aggregate by the effect of electrostatic attraction and adsorption bridging with the bacterial cell of charged load, strengthened the intensity of biological floe.The granule sludge degree of compactness height that forms, settling property is good.
Embodiment:
Embodiment 1:
Seed sludge adopts municipal sewage plant's digested sludge.
Adding polyquaternium is granular sludge promotor with the polyquaternium, and anaerobic reactor starts the back and adds polyquaternium with the dosing method that added once in per two days in reactor.Polyquaternium adds dosage with the estimation of sludge seeding amount, and both quality ratio is: polyquaternium/sludge quantity=1.6mg/g.
Substratum with carbohydrate waste water as substratum.
The initial OLR of control organic loading rate adopts 0.5gCOD/ (Ld), is the timed interval that prerequisite determines to improve OLR with COD clearance 85%, makes OLR be able to quick raising.
Alr mode and intensity adopt intermittently alr mode of strength, and stirring frequency is for stirring the every interval 1h of 5min/, and stirring intensity is that velocity slope square root G value is got 85s -1
Reactor configuration height for reactor and diameter ratio H/D get 5.
It is to keep the dominant important factor of sarcina methanica that micro-metals directly adds to Fe, Co, Ni salt compounds in the reactor, and micro-dosage is: Fe adopts 1mg/ (Ld); Co adopts 0.1mg/ (Ld); Ni adopts 0.2mg/ (Ld).
Embodiment 2:
Seed sludge adopts municipal sewage plant's digested sludge.
Adding polyquaternium is granular sludge promotor with the polyquaternium, and anaerobic reactor starts the back and adds polyquaternium with the dosing method that added once in per two days in reactor.Polyquaternium adds dosage with the estimation of sludge seeding amount, and both quality ratio is: polyquaternium/sludge quantity=3.2mg/g.
Substratum: with carbohydrate waste water is substratum.
The initial OLR of control organic loading rate adopts 0.5gCOD/ (Ld), is the timed interval that prerequisite determines to improve OLR with COD clearance 85%, makes OLR be able to quick raising.
Alr mode and intensity adopt the mechanical stirring mode, and stirring intensity is that velocity slope square root G value is got 85s -1
Reactor configuration height for reactor and diameter ratio H/D get 6.
Micro-metals directly adds to Fe, Co, Ni salt compounds in the reactor, and micro-dosage is: Fe adopts 1mg/ (Ld); Co adopts 0.1mg/ (Ld); Ni adopts 0.2mg/ (Ld).
Embodiment 3:
Seed sludge adopts municipal sewage plant's digested sludge.
Adding polyquaternium is granular sludge promotor with the polyquaternium, and anaerobic reactor starts the back and adds polyquaternium with the dosing method that added once in per two days in reactor.Polyquaternium adds dosage with the estimation of sludge seeding amount, and both quality ratio is: polyquaternium/sludge quantity=2mg/g.
Substratum is a substratum with carbohydrate waste water.
The initial OLR of control organic loading rate adopts 0.5gCOD/ (Ld), is the timed interval that prerequisite determines to improve OLR with COD clearance 85%, makes OLR be able to quick raising.
Alr mode and intensity adopt the waterpower alr mode, and stirring intensity is that velocity slope square root G value is got 85s -1
Reactor configuration height for reactor and diameter ratio H/D get 5.5.
Micro-metals directly adds to Fe, Co, Ni salt compounds in the reactor, and micro-dosage is: Fe adopts 1mg/ (Ld); Co adopts 0.1mg/ (Ld); Ni adopts 0.2mg/ (Ld).

Claims (1)

1, a kind of anaerobic grain sludge fast culture process, it is characterized in that it being that a kind of quick formation is the cultural method of the anaerobic grain sludge of dominant bacteria with the sarcina methanica, concrete processing method is: be granular sludge promotor with the polyquaternium, the solid state polyquaternium is mixed with the solution of 1% concentration, start the back at anaerobic reactor and add polyquaternium with the dosing method that added once in per two days in reactor, the quality ratio of polyquaternium and seed sludge is between 1.6~3.2mg/g; With chemical oxygen demand (COD) Chemical OxygenDemand-COD clearance control organic loading rate Orgenic Loading Rate-OLR, be stabilized in greater than 85% o'clock raising OLR between the starting period at the COD clearance; Fe, Co, Ni salt compounds are mixed with solution, directly add in the reactor,
Raw material:
Seed sludge: municipal sewage plant's digested sludge;
Substratum: with carbohydrate organic waste water as substratum;
Granular sludge promotor: polyquaternium;
Salt compounds: FeCl 2, CoCl 2And NiCl 2
Condition:
I, the stirring of employing strength, mechanical stirring or waterpower alr mode;
II, employing dosing method at interval add polyquaternium in anaerobic reactor;
III, initial OLR adopt 0.5gCOD/ (Ld), are the timed interval that prerequisite determines to improve OLR with COD clearance ≮ 85%;
IV, directly add to Fe, Co, Ni salt compounds in the reactor;
V, height for reactor and diameter ratio H/D get 5~6 and are advisable.
CNA2006100129516A 2006-07-14 2006-07-14 Fast culture process in anaerobic grain sludge Pending CN1887737A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNA2006100129516A CN1887737A (en) 2006-07-14 2006-07-14 Fast culture process in anaerobic grain sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNA2006100129516A CN1887737A (en) 2006-07-14 2006-07-14 Fast culture process in anaerobic grain sludge

Publications (1)

Publication Number Publication Date
CN1887737A true CN1887737A (en) 2007-01-03

Family

ID=37577017

Family Applications (1)

Application Number Title Priority Date Filing Date
CNA2006100129516A Pending CN1887737A (en) 2006-07-14 2006-07-14 Fast culture process in anaerobic grain sludge

Country Status (1)

Country Link
CN (1) CN1887737A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102219300A (en) * 2011-05-16 2011-10-19 苏州科技学院 Method for culturing anaerobic granular sludge in anaerobic baffled reactor
CN102557248A (en) * 2012-01-13 2012-07-11 西南化工研究设计院 Method for fast culturing anaerobic granular sludge
CN103043792A (en) * 2013-01-19 2013-04-17 东北电力大学 Method and device for cultivating anaerobic granular sludge
CN103159322A (en) * 2013-03-29 2013-06-19 威海百克环保工程有限公司 PTA (Pure Terephthalic Acid) sewage anaerobic sludge granulating accelerant
CN103265111A (en) * 2013-05-09 2013-08-28 华南理工大学 Anaerobic sludge granulating acceleration method
CN103771584A (en) * 2014-01-20 2014-05-07 西安工程大学 Anaerobic granular sludge and engineering fast culture method thereof
CN110550737A (en) * 2019-08-21 2019-12-10 万创青绿(北京)环境科技有限公司 Granular sludge preparation method and reactor
CN115557604A (en) * 2022-10-25 2023-01-03 江南大学 Method for quickly starting high-salinity organic wastewater anaerobic treatment reactor

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102219300A (en) * 2011-05-16 2011-10-19 苏州科技学院 Method for culturing anaerobic granular sludge in anaerobic baffled reactor
CN102557248A (en) * 2012-01-13 2012-07-11 西南化工研究设计院 Method for fast culturing anaerobic granular sludge
CN103043792B (en) * 2013-01-19 2014-05-21 东北电力大学 Method and device for cultivating anaerobic granular sludge
CN103043792A (en) * 2013-01-19 2013-04-17 东北电力大学 Method and device for cultivating anaerobic granular sludge
CN103159322A (en) * 2013-03-29 2013-06-19 威海百克环保工程有限公司 PTA (Pure Terephthalic Acid) sewage anaerobic sludge granulating accelerant
CN103159322B (en) * 2013-03-29 2014-04-09 威海百克环保工程有限公司 PTA (Pure Terephthalic Acid) sewage anaerobic sludge granulating accelerant
CN103265111A (en) * 2013-05-09 2013-08-28 华南理工大学 Anaerobic sludge granulating acceleration method
CN103771584A (en) * 2014-01-20 2014-05-07 西安工程大学 Anaerobic granular sludge and engineering fast culture method thereof
CN103771584B (en) * 2014-01-20 2015-04-08 西安工程大学 Anaerobic granular sludge and engineering fast culture method thereof
CN110550737A (en) * 2019-08-21 2019-12-10 万创青绿(北京)环境科技有限公司 Granular sludge preparation method and reactor
CN110550737B (en) * 2019-08-21 2022-04-29 万创青绿(北京)环境科技有限公司 Granular sludge preparation method and reactor
CN115557604A (en) * 2022-10-25 2023-01-03 江南大学 Method for quickly starting high-salinity organic wastewater anaerobic treatment reactor
CN115557604B (en) * 2022-10-25 2024-05-07 江南大学 Method for quickly starting high-salt organic wastewater anaerobic treatment reactor

Similar Documents

Publication Publication Date Title
CN106810019B (en) Enhanced phosphorus removal and sludge reduction type sewage treatment process
Fang Microbial distribution in UASB granules and its resulting effects
CN1887737A (en) Fast culture process in anaerobic grain sludge
CN110540292B (en) Enhanced synchronous nitrification and denitrification process for adding AHLs signal molecules into biological moving bed process
CN101962222B (en) Method for fast aerobic granulation of flocculent sludge in sequence batch reactor
CN103601341A (en) SBR (Sequencing Batch Reactor) and SBBR (Sequencing Biofilm Batch Reactor) municipal sewage high-efficiency biological treatment method and device based on anaerobic ammonia oxidation
CN112250176A (en) Device and method for realizing advanced nitrogen and phosphorus removal of municipal sewage by integrated shortcut nitrification coupled with anaerobic ammonia oxidation denitrification phosphorus removal
CN103601287A (en) Culture method of aerobic nitrosification granule sludge
CN101468849A (en) Method for rapidly cultivating aerobic particle sludge by load control technique
US20200156975A1 (en) Method of upgrading the activated sludge process based on functional suspended carriers in the wastewater biological treatment process
CN103343145A (en) Method for promoting anaerobic sludge fermentation to produce short-chain fatty acids by utilizing reduced iron powder
CN103112948B (en) Method for rapidly culturing autotrophic nitrogen removal granule sludge under conditions of low substrate concentration and high ascending velocity
Zhao et al. Application of biogas recirculation in anaerobic granular sludge system for multifunctional sewage sludge management with high efficacy energy recovery
CN108383239B (en) Integrated biological treatment process for shortcut nitrification anaerobic ammonia oxidation and phosphorus removal under intermittent aeration mode
CN113149213A (en) Device and method for rapidly culturing aerobic granular sludge and treating low-carbon-ratio municipal sewage
CN106587544B (en) Enhanced phosphorus removal and sludge reduction type sewage treatment device
CN214880538U (en) Device for rapidly culturing aerobic granular sludge and treating low-carbon-ratio urban sewage
CN100467402C (en) Upward flow type composite anaerobic hydrolysis and acidification treater, and method
CN113683192B (en) Device and method for culturing and enriching short-cut denitrification granular sludge for providing electron acceptor nitrite nitrogen for anaerobic ammonia oxidation
CN114835255A (en) Composite bioreactor based on iron-carbon carrier and preparation and sewage treatment method thereof
CN1217866C (en) Alcohol type fermenting organism desulfurization method for treating sulfate organic wastewater
CN101468852B (en) Method for aerobic synchronous nitration and denitrification of coking wastewater
CN113998846A (en) Efficient carbon adsorption coupled biological nitrogen and phosphorus removal sewage treatment device and method
CN108249725B (en) Method for producing methane by pre-fermenting and enhancing anaerobic digestion of excess sludge
CN216550030U (en) Efficient carbon adsorption coupling biological nitrogen and phosphorus removal sewage treatment device

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C12 Rejection of a patent application after its publication
RJ01 Rejection of invention patent application after publication