CN1403390A - Combined sewage treating process and apparatus - Google Patents
Combined sewage treating process and apparatus Download PDFInfo
- Publication number
- CN1403390A CN1403390A CN02134820A CN02134820A CN1403390A CN 1403390 A CN1403390 A CN 1403390A CN 02134820 A CN02134820 A CN 02134820A CN 02134820 A CN02134820 A CN 02134820A CN 1403390 A CN1403390 A CN 1403390A
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- China
- Prior art keywords
- sewage
- runner
- blodisc
- jet
- rotating shaft
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Abstract
The sewage treating process uses the residual kinetic energy of the sewage after jet aeration as the driving power to rotate the biological turnplate to realize the sewage treatment. The embodiment includes biological turnplate, tank, rotating wheel and jet ejector, the biological turnplate and the rotating wheel are mounted inside the tank, the turnplate is connected via the rotation mechanism to the shaft, and the jet ejector is set opposite to the rotating wheel and connected to the sewage pump. The present invention can realize jet aeration, sewage sucking and residual energy driving of the biological turnplate and thus has high sewage treating efficiency, powerful resistance to impact load, good mud depositing performance, low power consumption and low running cost.
Description
Technical field
The present invention relates to a kind of sewage disposal technology, particularly a kind of combined sewage treating process and device thereof that integrates jet-flow aeration and drive blodisc (tube).
Background technology
The blodisc sewage treatment process is one of existing biologic process for treating sewage, and traditional blodisc or biological drum are to be fixed on the transverse axis by less rotary disk of a plurality of mutual spacings or cylinder to constitute.They all are to do to rotate continuously by driven by motor disk or cylinder, the microbial film that is grown on disk or cylinder and the filler is alternately contacted with atmosphere with sewage, organic pollutant in the sewage is attracted on the disk or in the cylinder, oxygenolysis under the effect of aerobic microbiological (being microbial film), thereby reach the purpose of purifying waste water, as being in 97242354.0 the Chinese utility model patent disclosed " a kind of waste disposal plant " in the patent No. with biological drum (drum) of weighting material, the multi-stage biological rotating cylinder (drum) that adopts driven by motor to have weighting material exactly rotates, and microbial film is alternately contacted with atmosphere to carry out the purification of sewage with sewage.But; above-mentioned treatment unit and technology all only depend on the continuous rotation of disk or cylinder and sewage are contacted with atmosphere; do not take measures to increase the content of water oxygen; thereby usually can produce foul smell because of oxygen in water is not enough; wastewater treatment efficiency is exerted an adverse impact, also limited to the application of this sharp sewage treatment process.A kind of " multi-stage sewage disposal with biological rotating disks " also disclosed in the patent No. is 90105136.5 Chinese invention patent, this process using sewage drives blodisc, promptly adopt rotating disks equipment, sewage flows out as power from header tank blodisc is rotated; This technology can improve oxygenation capacity and increase purification function, simultaneously can conserver power source, reduce cost of sewage disposal; But this deadweight that utilizes sewage drives the occasion that the treatment process of blodisc uses very big restriction is arranged, it has enough potential energy because sewage need be promoted to higher position, this is comparatively inconvenience when implementing, and the oxidation effect of this sewage treatment process also remains to be improved in addition.
Summary of the invention
The objective of the invention is to overcome the shortcoming of prior art, a kind of combined sewage treating process that integrates jet-flow aeration and drive blodisc (tube) is provided.
Another object of the present invention is to provide a kind of sewage disposal associated plant of realizing above-mentioned technology.
Purpose of the present invention is achieved through the following technical solutions: this combined sewage treating process rotates the processing that realizes sewage with the remaining kinetic energy of sewage behind jet-flow aeration as power wheel drive blodisc (tube).
Described sewage by behind the jet ejectors aeration with high-velocity jet on runner bucket, promote runner and rotate, runner drives rotating shaft by transmission rig and rotates, thereby makes the blodisc (tube) that is fixed in the rotating shaft with certain speed rotation.
Described jet ejectors utilizes effluent cycle to spray and sucks fresh sewage, also suck fresh air by air suction inlet, and gas, water mix in the mixing section of jet ejectors, thereby reach the purpose of aeration.
Described blodisc and (or) biological drum is fixedly mounted in the rotating shaft with series system.
A kind of sewage disposal associated plant of realizing above-mentioned technology, comprise the blodisc (tube) that is fixed in the rotating shaft, also comprise cell body, runner, jet ejectors, blodisc (tube), rotating shaft, runner are installed in the cell body, runner is connected with rotating shaft by transmission rig, and jet ejectors is arranged on the position relative with runner and is connected with the sump pump of peripheral hardware.
Described jet ejectors comprises a flow inlet, a water sucking mouth, an air suction inlet and a jet orifice; Wherein, flow inlet is connected with sump pump by valve, and the water sucking mouth is connected with sewage lagoon by valve, and air suction inlet communicates with atmosphere by valve, and jet orifice is relative with runner; Jet ejectors is fixed on the cover plate of cell body, and its flow angle can be regulated by regulating mechanism, to realize the speed-regulating function of blodisc (tube).
Described cell body is separated into cyclic aeration groove, flow control groove and biochemical reaction groove three parts by dividing plate, in the cyclic aeration groove runner is installed, blodisc (tube) is installed in the biochemical reaction groove, is provided with adjustable overflow weir in the flow control groove and is connected with the biochemical reaction groove.
Have baffle plate to be divided into some unit in the described biochemical reaction groove, to form the plural serial stage reactive tank, blodisc (tube) lays respectively in each unit.
Described biological drum is welded by front and rear cover plate, rib, gusset, and the inner chamber of biological drum can be put into different fillers as required.
The disc of described blodisc can be selected for use as required.Both can be circular, also can be polygonal, both can be dull and stereotyped, also can be other form, and available steel plate or other material are made.
Described rotating shaft by sleeve and nut biological drum and (or) blodisc is cascaded, the rotating shaft two ends are equipped with bearing, by bearing rotating shaft and on rotating cylinder and rotating disk etc. be placed on the support that is welded in biochemical reaction groove two ends.
Action principle of the present invention is: under the dynamic action of sump pump, jet ejectors is when sucking sewage lagoon sewage, suck fresh air by air suction inlet, gas, water carry out spraying from jet orifice behind the mixed aeration in the mixing section of jet ejectors, high speed gas, water mixed liquid are injected on the runner bucket, the promotion runner rotates, and runner drives rotating shaft by transmission rig and rotates, thus make series connection be fixed in the rotating shaft biological drum and (or) blodisc rotates with certain speed.The gas that jet ejectors ejects, water mixed liquid act on the blade and reflect that part of, enter the flow control groove, through shunting, a part enters the biochemical reaction groove by adjustable overflow weir at this, rest part is back to the cyclic aeration groove; Because the biochemical reaction groove becomes several parts by barrier partitions, therefore, the sewage that enters the biochemical reaction groove can be along the circuitous biochemical reaction groove that flows through of formed runner.The part of biological drum and blodisc is immersed in the sewage of biochemical reaction groove, and rotates with certain speed; Alternately contact with sewage with air with microbial film on the blodisc attached to biological drum, the organic pollutant when flooding in the absorption sewage absorbs the oxygen in the atmosphere during worn-out revealing; Circulation makes the organic pollutant in the sewage obtain oxygenolysis under the effect of aerobic microbiological so repeatedly, and simultaneously, the microbial film on biological drum and the blodisc constantly comes off voluntarily, and the sewage after handling drains into settling tank to be separated; In addition, because the aeration effect of jet ejectors makes the sewage that enters the biochemical reaction groove maintain enough dissolved oxygens, guarantee that microorganism can breed vigorously.
The present invention compared with prior art has following advantage:
(1) thus this combined sewage treating process utilizes jet ejectors to realize jet-flow aeration, self-priming sewage simultaneously and promotes the effect that runner drives blodisc (tube) rotation with jet, having overcome prior art adopts that motor drive mode exists because not enough foul smell and the big shortcoming of equipment occupation of land of producing of dissolved oxygen greatly improved the purification efficiency to sewage; Simultaneously, drive the treatment process of blodisc with respect to the deadweight that utilizes sewage, application of the present invention is more convenient, not the restriction of elevation of water surface.
(2) this sewage disposal associated plant is rational in infrastructure, simplified structure with respect to prior biological rotating disk (tube) waste disposal plant, reduced composition member (device need not the electric motor driving member), do not need the adapted submersible sewage pump generally speaking, only use common sump pump to get final product, thereby saved investment and maintenance cost preferably.
(3) this sewage disposal associated plant combines the advantage of set growing technology and suspension growth technology, and with biological drum and blodisc optimum combination in an equipment, both promote each other, under same appointed condition (as disk diameter), wastewater purifying efficiency of this device and processing power are higher than common blodisc (tube), to have the anti impulsion load ability strong for this device simultaneously, advantage such as sludge settling property is good.
(4) the present invention so the power and energy saving has reduced working cost, and has improved wastewater purification efficiency, uses remarkable in economical benefits because of having utilized the remaining kinetic energy behind the jet-flow aeration as the power that drives blodisc (tube) for a long time, and application prospect is wider.
Description of drawings
Fig. 1 is the schema of combined sewage treating process of the present invention.
Fig. 2 is a front view of realizing the sewage disposal associated plant of combined sewage treating process shown in Figure 1.
Fig. 3 is the vertical view of waste disposal plant shown in Figure 2.
Fig. 4 is the side-view of waste disposal plant shown in Figure 2.
Embodiment
Below in conjunction with the embodiment accompanying drawing the present invention is done further concrete description.
Embodiment
Fig. 1 shows idiographic flow of the present invention, as seen from Figure 1, this sewage disposal combined system includes sump pump 18, sewage lagoon 19, waste disposal plant, valve 20 etc., wherein waste disposal plant comprises jet ejectors 15, and jet ejectors 15 comprises a flow inlet 15-1, water sucking mouth 15-2, an air suction inlet 15-3 and a jet orifice 15-4; Wherein, flow inlet 15-1 is connected with sump pump 18 by valve 20, and water sucking mouth 15-2 is connected with sewage lagoon 19 by valve 20, and air suction inlet 15-3 communicates with atmosphere by valve 20, and jet orifice 15-4 is relative with the runner 16 of waste disposal plant; Concrete technological process is: under the dynamic action of sump pump 18, jet ejectors 15 is when sucking sewage lagoon 19 sewage, also suck air by air suction inlet 15-3, gas, water mix the back and spray from jet orifice 15-4 in the mixing section of jet ejectors 15, rotate the biological drum 7 that drives waste disposal plants and blodisc 8 and rotate realizing processing thereby promote runner 16 sewage with certain speed, the sewage after the processing by row of conduits to settling tank.
Described waste disposal plant such as Fig. 2～shown in Figure 4, comprise cyclic aeration groove 1, Worm and worm-wheel gearing 2, cover plate 3, bearing 4, sleeve 5, nut 6, biological drum 7, blodisc 8, rotating shaft 9, baffle plate 10, biochemical reaction groove 11, flow control groove 12, adjustable overflow weir 13, rising pipe 14, jet ejectors 15, runner 16, return line 17; Being provided with adjustable overflow weir 13 in the flow control groove 12 is connected with biochemical reaction groove 11, cyclic aeration groove 1 is arranged on biochemical reaction groove 11 1 sides, cover plate 3 is installed above it, its inside is equipped with runner 16, runner 16 is welded on the wheel hub by a plurality of blades to be formed, with the runner 16 relative jet ejectors 15 that are equipped with, jet ejectors 15 is fixed on the cover plate 3 of cyclic aeration groove 1, its flow angle is adjustable, to realize the speed-regulating function of blodisc (tube), the flow inlet of jet ejectors 15 is connected with sump pump 18 by valve 20; Runner 16 is connected by the rotating shaft 9 in Worm and worm-wheel gearing 2 and the biochemical reaction groove 11, biological drum 7 and blodisc 8 are installed in the rotating shaft 9, biological drum 7 and blodisc 8 are positioned at the some unit that are separated into by baffle plate 10 of biochemical reaction groove 11, biological drum 7 is welded by front and rear cover plate, rib, gusset, the inner chamber of biological drum 7 can be put into the filler of different types as required, and blodisc 8 can be made with steel plate or other material; Rotating shaft 9 is cascaded biological drum 7 and blodisc 8 by sleeve 5 and nut 6, and rotating shaft 9 two ends are equipped with bearing 4, by bearing 4 rotating shaft 9 and on biological drum 7 and blodisc 8 etc. be placed on the support that is welded in biochemical reaction groove 11 two ends.
The foregoing description is preferred embodiment of the present invention; but embodiments of the present invention are not restricted to the described embodiments; other any do not deviate from change, the modification of being done under spirit of the present invention and the technology or substitutes; all should be the displacement of equivalence, be included within protection scope of the present invention.
Claims (8)
1, a kind of combined sewage treating process is characterized in that: rotate to realize the processing to sewage as power wheel drive blodisc (tube) with the remaining kinetic energy of sewage behind jet-flow aeration.
2, combined sewage treating process according to claim 1, it is characterized in that: described jet ejectors is when sucking sewage lagoon sewage, also suck fresh air by air suction inlet, gas, water mix the realization aeration in the mixing section of jet ejectors.
3, combined sewage treating process according to claim 1, it is characterized in that: the work of described sewage by jet ejectors in order to high-velocity jet on runner bucket, the promotion runner rotates, runner drives rotating shaft by transmission rig and rotates, and the blodisc (tube) that is fixed in the rotating shaft is rotated with certain speed.
4, combined sewage treating process according to claim 1 is characterized in that: described blodisc and (or) biological drum is fixedly mounted in the rotating shaft with series system.
5, a kind of sewage disposal associated plant, comprise the blodisc (tube) that is fixed in the rotating shaft, it is characterized in that: comprise cell body, runner (16), jet ejectors (15), blodisc (tube) (7,8), rotating shaft (9), runner (16) are installed in the cell body, runner (16) is connected with rotating shaft (9) by transmission rig, and jet ejectors (15) is arranged on and the relative position of runner (16).
6, sewage disposal associated plant according to claim 5 is characterized in that: described jet ejectors comprises a flow inlet (15-1), a water sucking mouth (15-2), an air suction inlet (15-3) and a jet orifice (15-4); Wherein, flow inlet (15-1) is connected with sump pump (18) by valve (20), water sucking mouth (15-2) is connected with sewage lagoon (19) by valve (20), and air suction inlet (15-3) communicates with atmosphere by valve (20), and jet orifice (15-4) is relative with runner (16).
7, sewage disposal associated plant according to claim 5, it is characterized in that: described cell body is separated into cyclic aeration groove (1), flow control groove (12) and biochemical reaction groove (11) three parts by dividing plate, runner (16) is installed in the cyclic aeration groove (1), blodisc (tube) (7,8) is installed in the biochemical reaction groove (11), is provided with adjustable overflow weir (13) in the flow control groove (12) and is connected with biochemical reaction groove (11).
8, sewage disposal associated plant according to claim 7 is characterized in that: have baffle plate (10) to be divided into some unit in the described biochemical reaction groove (11), blodisc (tube) (7,8) lays respectively in each unit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021348200A CN1180991C (en) | 2002-09-26 | 2002-09-26 | Combined sewage treating process and apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021348200A CN1180991C (en) | 2002-09-26 | 2002-09-26 | Combined sewage treating process and apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1403390A true CN1403390A (en) | 2003-03-19 |
| CN1180991C CN1180991C (en) | 2004-12-22 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB021348200A Expired - Fee Related CN1180991C (en) | 2002-09-26 | 2002-09-26 | Combined sewage treating process and apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1180991C (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1325395C (en) * | 2005-02-28 | 2007-07-11 | 东南大学 | Combined self-refluxing denitrogenating biological turntable |
| CN102350103A (en) * | 2011-08-31 | 2012-02-15 | 清华大学 | Water body purification device and water conveyance project system comprising the same |
| CN103145293A (en) * | 2013-01-15 | 2013-06-12 | 南京元凯生物能源环保工程有限公司 | Combined type biological rotating disk treatment device and method using same to treat sewage |
| CN105712469A (en) * | 2016-02-04 | 2016-06-29 | 东南大学 | Aerobic drum-type microbial film electrochemical reactor and application thereof |
| CN106995235A (en) * | 2017-05-31 | 2017-08-01 | 四川豪特实业集团有限公司 | One kind fluidisation rotating-drum biofilter |
| CN108178267A (en) * | 2018-03-14 | 2018-06-19 | 郑青飞 | A kind of rotary sewage disposal device based on baffle disturbance |
| CN108249536A (en) * | 2018-03-14 | 2018-07-06 | 郑青飞 | A kind of rotary sewage disposal device based on rotational speed regulation |
| CN108579402A (en) * | 2018-05-23 | 2018-09-28 | 扬州大学 | A kind of biological rotating disk organic waste gas treatment device |
| CN108793353A (en) * | 2018-05-25 | 2018-11-13 | 张秀英 | A kind of sewage disposal flocculation apparatus with fluid driving mixed function |
| CN111320329A (en) * | 2020-03-13 | 2020-06-23 | 李海洋 | Domestic sewage treatment device and treatment method |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1717208B1 (en) * | 2005-04-28 | 2013-06-26 | Grundfos Management A/S | Device for fluid treatment, in particular for waste water treatment, with a stack of discs |
-
2002
- 2002-09-26 CN CNB021348200A patent/CN1180991C/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1325395C (en) * | 2005-02-28 | 2007-07-11 | 东南大学 | Combined self-refluxing denitrogenating biological turntable |
| CN102350103A (en) * | 2011-08-31 | 2012-02-15 | 清华大学 | Water body purification device and water conveyance project system comprising the same |
| CN103145293A (en) * | 2013-01-15 | 2013-06-12 | 南京元凯生物能源环保工程有限公司 | Combined type biological rotating disk treatment device and method using same to treat sewage |
| CN105712469A (en) * | 2016-02-04 | 2016-06-29 | 东南大学 | Aerobic drum-type microbial film electrochemical reactor and application thereof |
| CN105712469B (en) * | 2016-02-04 | 2018-07-17 | 东南大学 | Aerobic drum-type microbial film electrochemical reactor and its application |
| CN106995235A (en) * | 2017-05-31 | 2017-08-01 | 四川豪特实业集团有限公司 | One kind fluidisation rotating-drum biofilter |
| CN108178267A (en) * | 2018-03-14 | 2018-06-19 | 郑青飞 | A kind of rotary sewage disposal device based on baffle disturbance |
| CN108249536A (en) * | 2018-03-14 | 2018-07-06 | 郑青飞 | A kind of rotary sewage disposal device based on rotational speed regulation |
| CN108579402A (en) * | 2018-05-23 | 2018-09-28 | 扬州大学 | A kind of biological rotating disk organic waste gas treatment device |
| CN108793353A (en) * | 2018-05-25 | 2018-11-13 | 张秀英 | A kind of sewage disposal flocculation apparatus with fluid driving mixed function |
| CN111320329A (en) * | 2020-03-13 | 2020-06-23 | 李海洋 | Domestic sewage treatment device and treatment method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1180991C (en) | 2004-12-22 |
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