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CN108911125A - A kind of novel upflow anaerobic sludge blanket reactor - Google Patents

A kind of novel upflow anaerobic sludge blanket reactor Download PDF

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Publication number
CN108911125A
CN108911125A CN201810789926.1A CN201810789926A CN108911125A CN 108911125 A CN108911125 A CN 108911125A CN 201810789926 A CN201810789926 A CN 201810789926A CN 108911125 A CN108911125 A CN 108911125A
Authority
CN
China
Prior art keywords
reactor
gas
anaerobic
sludge
distribution device
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
CN201810789926.1A
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Chinese (zh)
Inventor
李彦民
陈家轲
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.)
Suzhou Qing Qing Environmental Protection Technology Co Ltd
Original Assignee
Suzhou Qing Qing Environmental Protection Technology 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 Suzhou Qing Qing Environmental Protection Technology Co Ltd filed Critical Suzhou Qing Qing Environmental Protection Technology Co Ltd
Priority to CN201810789926.1A priority Critical patent/CN108911125A/en
Publication of CN108911125A publication Critical patent/CN108911125A/en
Pending legal-status Critical Current

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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
    • C02F3/28Anaerobic digestion processes
    • C02F3/2846Anaerobic digestion processes using upflow anaerobic sludge blanket [UASB] reactors
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F2001/007Processes including a sedimentation step
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2203/00Apparatus and plants for the biological treatment of water, waste water or sewage
    • C02F2203/006Apparatus and plants for the biological treatment of water, waste water or sewage details of construction, e.g. specially adapted seals, modules, connections

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

Abstract

The invention discloses a kind of novel upflow anaerobic sludge blanket reactors, including reactor body, water feed apparatus, distribution device, mud discharging device, effluent collection device, three separators, reaction zone, settling zones etc..After removing moisture removal, impurity by moisture trap, filter pretreatment by the gas that reactor is discharged, the release of reactor distribution device is entered back into booster fan pressurization, for stirring.It is stirred reactor is reinjected after the gas boosting of reactor discharge, can achieve waste water and the well-mixed purpose of anaerobic grain sludge, strengthened mass transfer effect, improve the treatment effect of reactor.Higher superficial gas upflow velocity and shearing force can be provided simultaneously, is more advantageous to the formation of anaerobic grain sludge.

Description

A kind of novel upflow anaerobic sludge blanket reactor
Technical field
The invention belongs to waste water treatment process, and in particular to a kind of novel upflow anaerobic sludge blanket reactor.
Background technique
Up-flow anaerobic sludge blanket(Upflow Anaerobic Sludge Blanket, abbreviation UASB)Reactor is lotus Blue Wageningen agriculture university Leuinga et al. is succeeded in developing between 1973-1977.China started upstream in 1981 The research work of formula anaerobic mud bed reactor.UASB technique has obtained the application of large-scale popularization in China at present, especially It is even more to have obtained sufficient application in terms of high concentrated organic wastewater processing.From the point of view of current engineering practice, UASB technique by It is in granular form state in its anaerobic sludge, it is allow to maintain higher sludge concentration in reactor compared to conventional anaerobic technique, Therefore handling it, organic volumetric loading is higher, and impact resistance ability is stronger.
Although the practice effect of current UASB technique is fine, but improved place in need.UASB Waste at present The mixing and stirring of water and anaerobic grain sludge are realized by the Gas Stirring of hydraulic mixing and the anaerobism generation of water inlet. Mainly stirred by the gas that anaerobism generates, but the gas that anaerobism generates must be limited, especially when organic volume is negative When lotus is low, the gas of generation is less, and the stirring action generated is also just weaker.Can waste water be sufficiently mixed directly with anaerobic sludge Influence the treatment effect of UASB technique.Now in order to strengthen being sufficiently mixed for waste water and anaerobic sludge, the method for use is to increase Add interior reflux, such as EGSB technique, is exactly to flow back by the way that increase is interior, i.e., it is useless to strengthen by strong water inlet hydraulic mixing Water and anaerobic sludge are sufficiently mixed.But energy consumption is high for hydraulic mixing, and mixed effect is also not highly desirable.
Summary of the invention
The object of the invention is to provide a kind of novel upflow anaerobic sludge to solve the defect of above-mentioned UASB technique Bed reactor.
The technical scheme is that:A kind of novel upflow anaerobic sludge blanket reactor, including reactor body, water inlet Device, mud discharging device, effluent collection device, distribution device, three phase separator, reaction zone, settling zone, it is characterized in that three phase separation The gas of device separation discharge enters moisture trap by pipeline and carries out gas-water separation, enters filter later and filters out in gas Impurity enters distribution device after entering back into booster fan pressurization.Distribution device discharges the gas of pressurization, and the gas of release exists Stirring action can be played during rising, and coming into full contact with and mixing for waste water and lonely granule sludge is reached with this. UASB reactor in the process of running, can continue to generate gas.In order to which extra gas to be discharged, it is equipped on exhaust line Safety valve, when its pressure is more than the setting value of safety valve, safety valve action discharges excessive gas.
Core of the invention thinking is exactly by gases such as the methane, the carbon dioxide that generate UASB reactor, and it is appropriate to do After pretreatment, into after booster fan adherence pressure, the gas distribution pipe release of UASB reactor is entered back into, the stirring by gas is made With to realize being sufficiently mixed for waste water and anaerobic grain sludge.Due to being that the gas generated by UASB reactor itself carries out Stirring, the environment in reactor will not be impacted.After the gas pressurized of UASB reactor, reinjecting reactor can compare Strong more of the gas agitating effect of existing UASB.Therefore can be provided for reactor higher superficial gas upflow velocity and Stronger shearing force, and the two conditions attain full and complete satisfaction, and are also easier to, faster realize the granulating of anaerobic sludge.
Waste water enters reaction zone by water feed apparatus, and makes the bottom that reactor body is uniformly distributed in into water.Waste water is reacting Area and the raw anaerobic reaction of anaerobic grain sludge hybrid concurrency, the gas that anaerobism generates are entered by the exhaust line of three phase separator Moisture separation removal in gas is entered filter later, filters out the impurity of gas by moisture trap, into booster fan, After being pressurized by blower, the gas of pressurization enters distribution device and is discharged again.During release, mistake of the gas in rising Disturbance is formed in journey, to realize that waste water is more fully mixed with anaerobic grain sludge.Gas enters air water point by three phase separator From device, filter, booster fan, reactor distribution device discharges again, enters back into three phase separator, is thusly-formed closed cycle. Gas is constantly generated since waste water is reacted with anaerobic grain sludge, pressure increase in pipeline can be made, when line pressure reaches certain After value, extra gas is discharged by safety valve.After the waste water of reaction zone is cleaned, into settling zone precipitation and separation, Clear waste water is discharged by effluent collection device.And excess sludge is discharged by mud discharging device.
Novel upflow anaerobic sludge blanket reactor of the present invention, by after the gas boosting that generates anaerobism, then It is filled with reactor, by the stirring repeatedly of gas, being sufficiently mixed for waste water and anaerobic grain sludge may be implemented, strengthen mass transfer effect Fruit improves treatment effect.Higher superficial gas upflow velocity and stronger shearing force can be provided for reactor simultaneously, more had Conducive to the granulating of anaerobic sludge.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of novel upflow anaerobic sludge blanket reactor of the present invention.
Wherein:1, reactor body;2, water feed apparatus;3, distribution device;4, mud discharging device;5, effluent collection device;6, Three phase separator;7, safety valve;8, moisture trap;9, filter;10, booster fan;11, settling zone;12, reaction zone.
Specific embodiment
The present invention is described in further detail below in conjunction with the accompanying drawings.
As shown in Figure 1, waste water enters reaction zone 12 by water feed apparatus 2, and make to be uniformly distributed in reactor body 1 into water Bottom.Waste water passes through three-phase separate in reaction zone 12 and the raw anaerobic reaction of anaerobic grain sludge hybrid concurrency, the gas that anaerobism generates Exhaust line from device 6 enters moisture trap 8, by moisture separation removal in gas, enters filter 9 later, filters out gas The impurity of body, into booster fan 10, after being pressurized by blower, the gas of pressurization enters distribution device 3 and is discharged again.It is releasing During putting, gas forms disturbance during rising, to realize that waste water is more fully mixed with anaerobic grain sludge.Gas Body enters moisture trap 8, filter 9 by three phase separator 6, increases blower 10 and reactor distribution device 3 discharges again, later Three phase separator 6 is entered back into, closed cycle is thusly-formed.Gas, meeting are constantly generated since waste water is reacted with anaerobic grain sludge Make pressure increase in pipeline, after line pressure reaches certain value, extra gas is discharged by safety valve 7.By reaction After the waste water in area is cleaned, into 11 precipitation and separation of settling zone, clear waste water is discharged by effluent collection device 5.It is remaining dirty Mud is discharged by mud discharging device 4.

Claims (1)

1. a kind of novel upflow anaerobic sludge blanket reactor, including reactor body(1), water feed apparatus(2), mud discharging device(4), Distribution device(3), effluent collection device(5), three phase separator(6), reaction zone(12), settling zone(11), it is characterized in that three-phase Separator(6)The gas of separation discharge enters moisture trap(8)Gas-water separation is carried out, enters filter later(9), enter back into Booster fan(10)Enter distribution device after pressurization(3), discharged, and safety valve is installed on exhaust line(7).
CN201810789926.1A 2018-07-18 2018-07-18 A kind of novel upflow anaerobic sludge blanket reactor Pending CN108911125A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810789926.1A CN108911125A (en) 2018-07-18 2018-07-18 A kind of novel upflow anaerobic sludge blanket reactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810789926.1A CN108911125A (en) 2018-07-18 2018-07-18 A kind of novel upflow anaerobic sludge blanket reactor

Publications (1)

Publication Number Publication Date
CN108911125A true CN108911125A (en) 2018-11-30

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810789926.1A Pending CN108911125A (en) 2018-07-18 2018-07-18 A kind of novel upflow anaerobic sludge blanket reactor

Country Status (1)

Country Link
CN (1) CN108911125A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109694130A (en) * 2019-03-08 2019-04-30 苏州科技大学 A kind of device and its application method realized sludge suspension and avoid sludge loss
CN112175801A (en) * 2019-07-01 2021-01-05 北京创臻环境技术有限公司 Uniform gas supply and heat circulation system

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1874964A (en) * 2003-10-29 2006-12-06 赫尔丁过滤技术有限公司 Reactor and method for anaerobic wastewater treatment
CN1986453A (en) * 2005-12-24 2007-06-27 张仁志 UASB biological pneumatic circulation stirring technique
CN102040280A (en) * 2010-12-10 2011-05-04 马翠忠 Pulse ejection internal-circulation anaerobic reactor
CN105330014A (en) * 2014-08-11 2016-02-17 上海羽利环保设备技术有限公司 Novel up-flow anaerobic sludge bed (UASB)
CN108101209A (en) * 2017-12-14 2018-06-01 华南理工大学 It is a kind of using sulfur-bearing iron chemical sludge to the method for waste water advanced denitrogenation

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1874964A (en) * 2003-10-29 2006-12-06 赫尔丁过滤技术有限公司 Reactor and method for anaerobic wastewater treatment
CN1986453A (en) * 2005-12-24 2007-06-27 张仁志 UASB biological pneumatic circulation stirring technique
CN102040280A (en) * 2010-12-10 2011-05-04 马翠忠 Pulse ejection internal-circulation anaerobic reactor
CN105330014A (en) * 2014-08-11 2016-02-17 上海羽利环保设备技术有限公司 Novel up-flow anaerobic sludge bed (UASB)
CN108101209A (en) * 2017-12-14 2018-06-01 华南理工大学 It is a kind of using sulfur-bearing iron chemical sludge to the method for waste water advanced denitrogenation

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109694130A (en) * 2019-03-08 2019-04-30 苏州科技大学 A kind of device and its application method realized sludge suspension and avoid sludge loss
CN109694130B (en) * 2019-03-08 2023-08-15 苏州科技大学 Device for realizing sludge suspension and avoiding sludge loss and use method thereof
CN112175801A (en) * 2019-07-01 2021-01-05 北京创臻环境技术有限公司 Uniform gas supply and heat circulation system

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Application publication date: 20181130