CN1541956A - Integrative processing plant for high concentration organic wasted water - Google Patents
Integrative processing plant for high concentration organic wasted water Download PDFInfo
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- CN1541956A CN1541956A CNA2003101005131A CN200310100513A CN1541956A CN 1541956 A CN1541956 A CN 1541956A CN A2003101005131 A CNA2003101005131 A CN A2003101005131A CN 200310100513 A CN200310100513 A CN 200310100513A CN 1541956 A CN1541956 A CN 1541956A
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Abstract
The present invention relates to one kind of integral high concentration waste water processing apparatus. The apparatus has aerobic baffle plate reactor, water collecting settling tank, aerobic reaction tank or biological contact oxidizing tank and settling tank connected via vertical baffle plates. The unique separating structure and the plug flow mode make each reactor capable of domesticating and culturing microbe colony adaptive to the water quality and environment condition. The present invention is favorable to utilizing the activity of the anaerobic bacteria colony, raising the processing effect and stability of the system and simplifying the system structure. The present invention has small coverage area, low system cost, low power consumption and no frost crack of pipeline.
Description
Technical field:
The present invention relates to a kind of wastewater treatment equipment, relate in particular to a kind of wastewater treatment equipment of integral type, be applicable to the processing of high concentrated organic wastewater.
Background technology:
At present, in high concentrated organic wastewater is handled, directly adopt anaerobism or aerobic biological treatment process all to be difficult to obtain the ideal effect, utilize the acidication section of anaerobic process then more and more to be paid attention to as the A/O technology of front-end processing.Along with to the deepening continuously and the develop rapidly of various high efficiency anaerobic reactors of anaerobic digestion mechanism research, the Anaerobic Microbiological Treatment Technology of waste water has become one of core technology of resource and environment protection.UASB be the people such as Lettinga of Dutch Wageningen agriculture university in a kind of high efficiency anaerobic reactor of the exploitation seventies in 20th century, be widely used in production practice at present.The success of UASB has greatly promoted the development of other high efficiency anaerobic reactor, baffling type anaerobic reactor (Anaerobic Baffled Reactor, be called for short ABR) a kind of new and effective anaerobic reactor on the UASB basis, developed just, it have shortly flow, do not stop up, need not to stir, the easy characteristics of startup.
The ABR reactor is a kind of new high-efficiency anaerobic reactor that is proposed in early 1980s by the people such as McCarty of U.S. Stanford university.Some vertical flow deflectors are set in this reactor, reactor is separated into placed in-line several reaction, each reaction chamber can be regarded a relatively independent upflow sludge blanket system (Upflow sludge bed is called for short USB) as.The cellular structure of ABR reactor uniqueness and pulling flow type fluidised form make and can inoculate and culture out and flow to the sewage quality in this reaction chamber, the microflora that envrionment conditions adapts in each reaction chamber, thereby cause anaerobic reaction produce acid mutually and the product methane journey of handing down separated, make the ABR reactor on overall performance, be equivalent to a diphasic anaerobic treatment system.It is generally acknowledged that diphasic anaerobic technique is by producing the acid phase and producing separating of methane phase, two big class anaerobic bacteria floras can be grown under the optimum envrionment conditions separately, help giving full play to the activity of anaerobic bacteria flora, improve the treatment effect of system and the stability of operation.A weak point of ABR reactor is that system's effluent quality is relatively poor, and needing usually could qualified discharge through subsequent disposal.
The Cheng Kaiying of the Zhongshan city refined environment-friendly engineering of perseverance company and Liao Geyu handle the food dressing high concentrated organic wastewater with aerobic reaction tank and anaerobic reation pool (ABR-SBR) combination process July calendar year 2001, and every index of handling the back water outlet reaches the primary standard standard of G B 8978-1996.The Xu Yudong of Fujian Province environment protection designing institute; in May, 2002; water quality characteristics at woollen blanket waste water; adopt coagulating sedimentation-anaerobic baffle plate reaction tank-two-stage aerobic biochemical process to handle woollen blanket waste water; show through engineering practice; this technology advanced person, efficient, stable, water outlet can reach " textile dyeing and finishing industrial water pollution thing emission standard " (GB42 87-92) primary standard.But, the ABR-SBR combination process is because the water outlet of ABR reactor pumps into water collecting basin through pump, the water outlet of water collecting basin pumps into sbr reactor pond or biological contact oxidation pond through pump, the water outlet of sbr reactor pond or biological contact oxidation pond pumps into the coagulating sedimentation sand filter through pump, the consumption of pump and water pipe is many like this, make the structure of system numerous and diverse, floor space is big, and the energy consumption during system's operation is many, thereby has increased the cost of system greatly.
Summary of the invention:
The object of the present invention is to provide a kind of efficient, energy-conservation, take up an area of less, the high concentrated organic wastewater treatment unit of simple in structure, integral type that cost is low.
Purpose of the present invention realizes by following measure:
A kind of integral type high concentrated organic wastewater treatment unit, the anaerobic reaction chamber, aerobic reaction chamber and the settling chamber that are separated into by traverse baffle form, and bind in wherein said anaerobic reaction chamber, and described settling tank, aerobic reaction chamber are uncovered.
Described aerobic reaction chamber is provided with venting port, and the settling chamber is provided with sewage draining exit, and the aerobic reaction chamber is provided with inflation inlet.
Described flow deflector is perpendicular to above-mentioned each reaction chamber.
Described anaerobic reaction chamber is 3-5, and described settling chamber is at least 2.
Described each reaction chamber is followed successively by placed in-line anaerobic reaction chamber, settling chamber, aerobic reaction chamber, settling chamber along water (flow) direction.
Described aerobic reaction chamber is upflowing, downflow system reaction chamber.
Described anaerobic reaction chamber, aerobic reaction chamber, settling tank are rectangular parallelepiped.
The big I of above-mentioned each reaction chamber is specifically determined according to the concentration and the hydraulic load of former water.
The present invention compared with prior art has the following advantages:
1, efficient: the cellular structure of uniqueness of the present invention and pulling flow type fluidised form make and can inoculate and culture out and flow to the sewage quality in this reaction chamber, the microflora that envrionment conditions adapts in each reaction chamber, help giving full play to the activity of anaerobic bacteria flora, the treatment effect of raising system and the stability of operation, it is relatively poor to have overcome ABR reactive system effluent quality, needs the shortcoming through subsequent disposal ability qualified discharge usually.The total clearance that experimental results show that integral type high concentrated organic wastewater treatment unit of the present invention is 94.89%, and water outlet reaches the water quality requirement of Dry crop in " agricultural irrigation water quality standard ".
2, energy-conservation: the present invention adopt vertical traverse baffle with reactor be separated into the ABR reactor, the settling tank that catchments, sbr reactor pond or biological contact oxidation pond, settling tank, make it into as a whole, not only simplified system architecture, reduced floor space, and at least three pumps of saving and corresponding water pipe, reduce the cost of system, saved the energy consumption of system.
3, anti-bursting by freezing: the used pipeline of the present invention is few, and waste water flows into next reaction chamber from a reaction chamber by flow deflector, has effectively avoided the heat radiation of water pipe, can prevent the bursting by freezing of water pipe in winter.
4, be adapted to seasonality or biological wastewater treatment that batch production produced: in each chamber of reactor of the present invention, difference start time of the different microorganisms population that is survived under the varying environment.Microorganism culturing in the anaerobic room is the slowest, but anaerobic species can keep its biological activity and good sedimentation function more than at least one year under the condition that stop to supply with waste water and nutrition.So after this reactor start-up was good, when being no more than 1 year pitch time, biological activity was recovered when recovering to supply with waste water thereupon.
5, the toxic substance in impact load of the present invention and the water inlet has good buffering adaptive faculty, but heavy-duty service.
Description of drawings
Fig. 1 is that the present invention is the structure and the schema of downflow system aerobic reaction chamber
Fig. 2 is that the present invention is the structure and the schema of upflowing aerobic reaction chamber
4-settling chamber, 3-aerobic reaction chamber, 1-flow deflector 2-anaerobic reaction chamber
5-venting port 6-sewage draining exit 7-inflation inlet
The expression water (flow) direction
Embodiment
Embodiment 1: with reference to Fig. 1, a kind of integral type high concentrated organic wastewater treatment unit is the rectangular parallelepiped reaction tank that length is respectively 72cm, 20cm, 36cm, three anaerobic reaction chambers being divided into by vertical traverse baffle 1 average mark 2, a downflow system aerobic reaction chamber 3 and two settling chambers 4 form, and above-mentioned each reaction chamber is followed successively by placed in-line anaerobic reaction chamber, settling chamber, aerobic reaction chamber, settling chamber along water (flow) direction.Wherein bind and be provided with venting port 5 at its top in anaerobic reaction chamber 2; Settling tank 4, aerobic reaction chamber 3 are uncovered, and the lower curtate of settling chamber 4 is provided with sewage draining exit 6, and the sidewall of aerobic reaction chamber 3 is provided with inflation inlet 7.Adopt downflow system aerobic reaction chamber can make the aqueous vapor full contact help reaction, but the gas of water body is isolated imprecision with anaerobic room in settling chamber and the aerobic room, influences the reaction of anaerobic room.
Embodiment 2: with reference to Fig. 2, a kind of integral type high concentrated organic wastewater treatment unit is the rectangular parallelepiped reaction tank that length is respectively 72cm, 20cm, 36cm, three anaerobic reaction chambers being divided into by vertical flow deflector 1 average mark 2, a upflowing aerobic reaction chamber 3 and two settling chambers 4 form, and above-mentioned each reaction chamber is followed successively by placed in-line anaerobic reaction chamber, settling chamber, aerobic reaction chamber, settling chamber along water (flow) direction.Wherein bind and be provided with venting port 5 at its top in anaerobic reaction chamber 2; Settling tank 4, aerobic reaction chamber 3 are uncovered, and the lower curtate of settling chamber 4 is provided with sewage draining exit 6, and the sidewall of aerobic reaction chamber 3 is provided with inflation inlet 7.Adopt upflowing aerobic reaction chamber to overcome in the downflow system aerobic reaction chamber in the settling chamber and aerobic room the gas of water body and isolate imprecise shortcoming with anaerobic room, but aqueous vapor in the same way, microbial reaction is insufficient.
Waste water enter this device back along flow deflector up and down baffling advance, Sludge Bed by placed in-line anaerobic reaction chamber successively, organic substrate in the waste water is by obtaining removing with fully contacting of microorganism, by means of the effect that waste water flows and biogas rises, mud in the reaction chamber moves up and down, but since flow deflector stop and the settling property of mud self that mud flow velocity in the horizontal direction is extremely slow, thereby a large amount of anaerobic sludges is trapped, and discharges by the settling chamber; After the reaction bed that water body enters the aerobic reaction chamber through the settling chamber reacts, discharge from the top of settling chamber, the mud of generation etc. are discharged from the lower curtate of settling chamber.
Claims (7)
1, a kind of integral type high concentrated organic wastewater treatment unit, the anaerobic reaction chamber, aerobic reaction chamber and the settling chamber that are separated into by traverse baffle form, and bind in wherein said anaerobic reaction chamber, and described settling tank, aerobic reaction chamber are uncovered.
2, integral type high concentrated organic wastewater treatment unit as claimed in claim 1, it is characterized in that: described aerobic reaction chamber is provided with venting port, and the settling chamber is provided with sewage draining exit, and the aerobic reaction chamber is provided with inflation inlet.
3, integral type high concentrated organic wastewater treatment unit as claimed in claim 1, it is characterized in that: described traverse baffle is perpendicular to each reaction chamber.
4, integral type high concentrated organic wastewater treatment unit as claimed in claim 1 is characterized in that: described anaerobic reaction chamber is 3-5, and described settling chamber is at least 2.
5, as claim 1,2,3,4 described any integral type high concentrated organic wastewater treatment unit, it is characterized in that: described each reaction chamber is followed successively by placed in-line anaerobic reaction chamber, settling chamber, aerobic reaction chamber, settling chamber along water (flow) direction.
6, as claim 1,2,3,4 described any integral type high concentrated organic wastewater treatment unit, it is characterized in that: described aerobic reaction chamber is upflowing reaction chamber or downflow system reaction chamber.
7, as claim 1,2,3,4 described any integral type high concentrated organic wastewater treatment unit, it is characterized in that: described anaerobic reaction chamber, aerobic reaction chamber, settling tank are rectangular parallelepiped.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2003101005131A CN1541956A (en) | 2003-10-08 | 2003-10-08 | Integrative processing plant for high concentration organic wasted water |
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| Application Number | Priority Date | Filing Date | Title |
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| CNA2003101005131A CN1541956A (en) | 2003-10-08 | 2003-10-08 | Integrative processing plant for high concentration organic wasted water |
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| CN1541956A true CN1541956A (en) | 2004-11-03 |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100375724C (en) * | 2006-05-31 | 2008-03-19 | 清华大学 | Baffle-board reactor and method for treating sewage by using it |
| CN102861461A (en) * | 2011-12-31 | 2013-01-09 | 江苏兴达钢帘线股份有限公司 | Steel wire pretreatment washing water purification and recycling device |
| CN103316509A (en) * | 2012-03-22 | 2013-09-25 | 刘宪武 | Guide wall equipped storage pond |
| CN103922548A (en) * | 2014-05-04 | 2014-07-16 | 北京航空航天大学 | Biological reaction device for culturing high-oil microalgae by using wastewater |
| CN103951062A (en) * | 2014-05-04 | 2014-07-30 | 中国石油大学(北京) | Anaerobic-aerobic baffled reactor |
| CN111203008A (en) * | 2020-01-08 | 2020-05-29 | 广东富源科技股份有限公司 | Efficient multistage precipitation tank of sapphire crystal processing equipment coolant liquid powder |
-
2003
- 2003-10-08 CN CNA2003101005131A patent/CN1541956A/en active Pending
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100375724C (en) * | 2006-05-31 | 2008-03-19 | 清华大学 | Baffle-board reactor and method for treating sewage by using it |
| CN102861461A (en) * | 2011-12-31 | 2013-01-09 | 江苏兴达钢帘线股份有限公司 | Steel wire pretreatment washing water purification and recycling device |
| CN103316509A (en) * | 2012-03-22 | 2013-09-25 | 刘宪武 | Guide wall equipped storage pond |
| CN103316509B (en) * | 2012-03-22 | 2014-10-29 | 刘宪武 | Guide wall equipped storage pond |
| CN103922548A (en) * | 2014-05-04 | 2014-07-16 | 北京航空航天大学 | Biological reaction device for culturing high-oil microalgae by using wastewater |
| CN103951062A (en) * | 2014-05-04 | 2014-07-30 | 中国石油大学(北京) | Anaerobic-aerobic baffled reactor |
| CN103951062B (en) * | 2014-05-04 | 2016-02-17 | 中国石油大学(北京) | A kind of anaerobic-aerobic baffled reactor |
| CN111203008A (en) * | 2020-01-08 | 2020-05-29 | 广东富源科技股份有限公司 | Efficient multistage precipitation tank of sapphire crystal processing equipment coolant liquid powder |
| CN111203008B (en) * | 2020-01-08 | 2021-11-19 | 广东富源科技股份有限公司 | Efficient multistage precipitation tank of sapphire crystal processing equipment coolant liquid powder |
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