CN109293139A - A kind of low cost integrated treatment high concentrated organic wastewater device - Google Patents

A kind of low cost integrated treatment high concentrated organic wastewater device Download PDF

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Publication number
CN109293139A
CN109293139A CN201811170950.3A CN201811170950A CN109293139A CN 109293139 A CN109293139 A CN 109293139A CN 201811170950 A CN201811170950 A CN 201811170950A CN 109293139 A CN109293139 A CN 109293139A
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CN
China
Prior art keywords
dredge
valve
integrated apparatus
level
limit
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Application number
CN201811170950.3A
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Chinese (zh)
Inventor
张慧
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Xuzhou University of Technology
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Xuzhou University of Technology
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Priority to CN201811170950.3A priority Critical patent/CN109293139A/en
Publication of CN109293139A publication Critical patent/CN109293139A/en
Withdrawn legal-status Critical Current

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    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00—Multistage treatment of water, waste water or sewage
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
    • C02F1/004—Processes for the treatment of water whereby the filtration technique is of importance using large scale industrial sized filters
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5209—Regulation methods for flocculation or precipitation
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00—Apparatus for treatment of water, waste water or sewage
    • C02F2201/002—Construction details of the apparatus
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00—General aspects of water treatment
    • C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/02—Aerobic processes
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/28—Anaerobic digestion processes

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  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Treatment Of Sludge (AREA)

Abstract

The invention discloses a kind of inexpensive integrated treatment high concentrated organic wastewater devices, and wherein limit for height air valve includes: limit for height valve manhole appendix, pressure sensor, limit for height valve air flue, limit for height valve air inlet, air valve pass valve, closes valve control line packet, closes valve axis, inner plenum；The limit for height valve manhole appendix and limit for height valve air inlet are located at limit for height air valve both ends, limit for height valve manhole appendix and limit for height valve air inlet and are mutually communicated by limit for height valve air flue；Inner plenum is equipped with inside limit for height air valve；It is equipped in the middle part of inner plenum and closes valve control line packet, to close airtight structure, and inner plenum is divided into two independent inner plenums, two independent inner plenums can only just be able to achieve perforation by limit for height valve air flue；It is equipped at the limit for height valve air flue central axes and closes valve axis, the two is slidably connected.The apparatus structure is rationally compact, and wastewater treatment efficiency is good, and cost is relatively low；The device piston is prepared using high molecular material, and mixing velocity enhancing rate is high.

Description

A kind of low cost integrated treatment high concentrated organic wastewater device
Technical field
The invention belongs to field of environment protection equipment, and in particular to a kind of low cost integrated treatment high concentrated organic wastewater dress It sets.
Background technique
With the development of economy, pesticide, chemical fertilizer be widely used and the increase of industrial wastewater discharge amount, make largely to contain Nitrogen and other biological nutrients matter are constantly discharged into river and lake and reservoir, make water body eutrophication degree accelerate to aggravate, at present China Industrial wastewater discharge amount is big and sewage is effectively treated that rate is low, and water pollution is serious, and processing is difficult to be up to state standards.
Although China has had taken up a large amount of measures to solve trade effluent pollution problem, deposited in terms of technical equipment The problems such as capital construction cost and operating cost are higher, treatment effeciency is to be improved.
Summary of the invention
In order to solve the above-mentioned technical problem, the present invention relates to a kind of inexpensive integrated treatment high concentrated organic wastewaters to fill It sets, comprising: integrated apparatus surge tank 1, sewage pump 2, outer sludge-discharge pipe 3, sludge water filter 4, sludge from sedimentation tank pipe 5 return Flow sludge pump 6, Central Control Center 7, reflux sludge tube 8, integrated apparatus bracket 9, sewage inlet pipe 10, level-one anoxic pond 11, level-one aerobic tank 12, level-one anaerobic pond 13, second level anoxic pond 14, secondary anaerobic pond 15, integrated apparatus sedimentation basin 16, two Grade aerobic tank 17, integrated apparatus filter tank 18, sterilization pool 19；The integrated apparatus bracket 9 is consistent vertical by 8 shape sizes Column connects and composes and is respectively formed the two slot rooms in left and right, and left side groove chamber interior is successively arranged level-one anaerobic pond 13, level-one anoxic pond 11, level-one aerobic tank 12, second level anoxic pond 14 and secondary anaerobic pond 15, right side groove chamber interior be successively arranged second level aerobic tank 17, Integrated apparatus sedimentation basin 16, integrated apparatus filter tank 18 and sterilization pool 19；The level-one of the level-one anaerobic pond 13 and one side Anoxic pond 11 is penetrated through by pipeline and is connected, and the right side of level-one anaerobic pond 13 is fixedly connected with second level anoxic pond 14；The level-one lacks Oxygen pond 11 is connected with the level-one aerobic tank 12 of one side, the perforation of right side secondary anaerobic pond 15 respectively by different pipelines；Described one Grade aerobic tank 12 is connected by pipeline and the perforation of second level anoxic pond 14；The second level aerobic tank 17 is located at integrated apparatus bracket 9 Right side groove room upper left side, 17 side of second level aerobic tank are respectively equipped with integrated apparatus sedimentation basin 16 and integrated apparatus filter tank 18, Second level aerobic tank 17 is connected with second level anoxic pond 14 and the perforation of integrated apparatus sedimentation basin 16 respectively by different pipelines；Described one Body makeup sets sedimentation basin 16 and integrated apparatus filter tank 18 and penetrates through connection by pipeline；The sterilization pool 19 is arranged in integrated makeup It sets 9 right side groove room right end of bracket, sterilization pool 19 and integrated apparatus filter tank 18 and connection is penetrated through by pipeline；The sludge from sedimentation tank One end perforation of pipe 5 is connected to the lower section of integrated apparatus sedimentation basin 16, the other end port of sludge from sedimentation tank pipe 5 respectively with reflux Sludge pipe 8 and the perforation connection of outer sludge-discharge pipe 3；Described 8 one end of reflux sludge tube respectively with level-one anaerobic pond 13, level-one anoxic pond 11 perforation connections, reflux sludge tube 8 are connected by return sludge pump 6 and the perforation of sludge from sedimentation tank pipe 5；The return sludge pump 6 It is connected by conducting wire with the control of Central Control Center 7；The sludge water filter 4 is set to outer 3 front end of sludge-discharge pipe, sludge water mistake Filter 4 and outer sludge-discharge pipe 3 penetrate through；The sewage inlet pipe 10 is set to 9 external upper of integrated apparatus bracket, sewage inlet pipe 10 one end are connected with level-one anaerobic pond 13 and the perforation of second level anoxic pond 14 respectively, and 10 other end of sewage inlet pipe passes through sewage pump 2 It penetrates through and connects with the integrated apparatus surge tank 1 on 9 right side of integrated apparatus bracket；The sewage pump 2 and Central Control Center 7 are logical Cross polygon control survey connection.
Further, this section is the explanation to heretofore described 16 structure of integrated apparatus sedimentation basin.The integration Device sedimentation basin 16 includes: bed mud delivery pipe 16-1, floater dragging device jacking system 16-2, tapered bed mud collecting tank 16- 3, integrated apparatus sedimentation basin bracket 16-4, clean water chamber 16-5, floater dragging device 16-6, the water inlet of integrated apparatus sedimentation basin Pipe 16-7, integrated apparatus sedimentation basin secondary treatment system 16-8；It is characterized in that, the integrated apparatus sedimentation basin bracket Floater dragging device 16-6 and clean water chamber 16-5 is equipped with inside 16-4, and floater dragging device 16-6 is located at clean water chamber 16-5 Top, integrated apparatus sedimentation basin bracket 16-4 are fixedly connected with clean water chamber 16-5, integrated apparatus sedimentation basin bracket 16-4's Quantity is 4, parallel between adjacent integrated apparatus sedimentation basin bracket 16-4 and be fixedly connected by horizontal truss；The floating Object marine salvage equipment jacking system 16-2 is located at integrated apparatus sedimentation basin bracket 16-4 inner wall upper end and the two is fixedly connected, floating The object marine salvage equipment side jacking system 16-2 is slidably connected with floater dragging device 16-6；The bottom of the clean water chamber 16-5 is set There is a tapered bed mud collecting tank 16-3, clean water chamber 16-5 and tapered bed mud collecting tank 16-3 surrounding seamless welding simultaneously penetrate through, clean water chamber The side of 16-5 and integrated apparatus sedimentation basin secondary treatment system 16-8 are penetrated through, and clean water chamber 16-5 is hollow cuboid knot Structure；The lower end of the tapered bed mud collecting tank 16-3 is disposed with bed mud delivery pipe 16-1, and the two penetrates through；The integrated apparatus Sedimentation basin water inlet pipe 16-7 is located at 16 top of integrated apparatus sedimentation basin.
Further, this section is the explanation to heretofore described floater dragging device jacking system 16-2 structure.Institute Stating floater dragging device jacking system 16-2 includes: lifting air pump 16-2-1, gas bleeder valve 16-2-2, air flue 16-2-3, high pressure Chamber 16-2-4, piston 16-2-5, elevating lever 16-2-6, limit for height air valve 16-2-7；The gas bleeder valve 16-2-2 is located at lifting air It pumps between 16-2-1 and air flue 16-2-3, the one end gas bleeder valve 16-2-2 and lifting air pump 16-2-1 perforation connect, gas bleeder valve 16-2- 2 other ends and air flue 16-2-3 perforation connect；The lifting air pump 16-2-1 is connect by conducting wire with Central Control Center 7；Institute State the other end and the seamless perforation of high-pressure chamber 16-2-4 of air flue 16-2-3；Piston is equipped with inside the high-pressure chamber 16-2-4 16-2-5 and elevating lever 16-2-6, high-pressure chamber's 16-2-4 outer wall lower end are equipped with limit for height air valve 16-2-7, high-pressure chamber 16-2-4 For hollow cylindrical structure；The piston 16-2-5 is slidably connected with high-pressure chamber's 16-2-4 inner wall, and piston 16-2-5's is straight Diameter is 3cm~5cm；The elevating lever 16-2-6 is located at piston lower portion and the two connects, and the diameter of elevating lever 16-2-6 is less than height Press the diameter of chamber 16-2-4；The limit for height air valve 16-2-7 and high-pressure chamber 16-2-4 perforation connects.
Further, this section is the explanation to heretofore described clean water chamber 16-5 structure.The limit for height air valve 16-2-7 It include: limit for height valve manhole appendix 16-2-7-1, pressure sensor 16-2-7-2, limit for height valve air flue 16-2-7-3, limit for height valve air inlet 16-2-7-4, air valve close valve 16-2-7-5, close valve control line packet 16-2-7-6, close valve axis 16-2-7-7, internal gas Room 16-2-7-8；The limit for height valve manhole appendix 16-2-7-1 and limit for height valve air inlet 16-2-7-4 are located at limit for height air valve 16- The both ends 2-7, limit for height valve manhole appendix 16-2-7-1 and limit for height valve air inlet 16-2-7-4 are mutual by limit for height valve air flue 16-2-7-3 Perforation；Inner plenum 16-2-7-8 is equipped with inside limit for height air valve 16-2-7；It is equipped in the middle part of inner plenum 16-2-7-8 and closes gas Gate control line packet 16-2-7-6, to close airtight structure, and by inner plenum 16-2-7-8 be divided into two it is independent in Portion gas chamber 16-2-7-8, two independent inner plenum 16-2-7-8 can only be just able to achieve by limit for height valve air flue 16-2-7-3 to be passed through It is logical；It is equipped at the central axes the limit for height valve air flue 16-2-7-3 and closes valve axis 16-2-7-7, the two is slidably connected, and closes in valve Axis 16-2-7-7 is electromagnetic structure, closes the one end valve axis 16-2-7-7 and is fixedly connected with air valve pass valve 16-2-7-5, works as gas Valve pass valve 16-2-7-5 is moved to close airtight when left side is bonded with pass valve control line packet 16-2-7-6；The pressure sensing Device 16-2-7-2 is located at the side limit for height air valve 16-2-7, and pressure sensor 16-2-7-2 is connected by conducting wire and Central Control Center 7 It connects；The pass valve control line packet 16-2-7-6 is connect by conducting wire with Central Control Center 7.
Further, this section is the explanation to heretofore described clean water chamber 16-5 structure.The clean water chamber 16-5 includes: Clean water chamber frame 16-5-1, aerofoil profile dispersion plate 16-5-2, rectangular slow drop plate 16-5-3 delay drop net 16-5-4, COD sensor 16- 5-5, overflow port 16-5-6；Aerofoil profile dispersion plate 16-5-2, rectangular slow drop plate 16-5- are equipped with inside the clean water chamber frame 16-5-1 3 gentle drop net 16-5-4；The clean water chamber frame 16-5-1 is hollow cylinder structure；The aerofoil profile dispersion plate 16-5-2 is located at side Shape is slow to drop the top plate 16-5-3 and is in different shaft staggered distributions, the quantity of aerofoil profile dispersion plate 16-5-2 from rectangular slow drop plate 16-5-3 It is 3, aerofoil profile dispersion plate 16-5-2 horizontal parallel arranges and both ends are fixedly connected with the inner wall of clean water chamber 16-5, adjacent aerofoil point The 16-5-2 that falls apart is in be equally spaced；The distance of the slow drop net 16-5-4 positioned at the rectangular slow drop lower part plate 16-5-3 and between the two For 13cm~18cm；The quantity of the rectangular slow drop plate 16-5-3 is 4, rectangular slow drop plate 16-5-3 horizontal parallel arrangement and two End is fixedly connected with the inner wall of clean water chamber 16-5, and for the slow drop plate 16-5-3 of adjacent prismatic in being equally spaced, adjacent prismatic delays drop plate 16- The distance between 5-3 is 5cm~10cm；The overflow port 16-5-6 is arranged in the upper end clean water chamber frame 16-5-1, overflow port 16- 5-6 is penetrated through by clean water chamber frame 16-5-1 and bed mud delivery pipe 16-1；The COD sensor 16-5-5 is arranged in clean water chamber 16-5 inner wall side, COD sensor 16-5-5 are connected by conducting wire and the control of Central Control Center 7.
Further, this section is the explanation to heretofore described floater dragging device 16-6 structure.The floating material Marine salvage equipment 16-6 includes: to salvage motor 16-6-1, salvages cam 16-6-2, salvages drive rod 16-6-3, salvages the 16-6- that cranks arm 4, crankshaft 16-6-5, steel wire slack adjuster 16-6-6 are salvaged, steel wire 16-6-7 is salvaged；The salvaging motor 16-6-1 is located at The upper end floater dragging device 16-6 is simultaneously fixedly connected with mono- side stand of floater dragging device 16-6, salvages motor 16-6-1's One end, which is equipped with, salvages cam 16-6-2, salvages motor 16-6-1 and salvages cam 16-6-2 transmission connection；The salvaging cam 16- 6-2 periphery upper end, which is equipped with, salvages drive rod 16-6-3, and it is different from one end of drive rod 16-6-3 is salvaged to salvage cam 16-6-2 Axis rotation connection, the diameter for salvaging cam 16-6-2 is 5cm~10cm；The quantity for salvaging drive rod 16-6-3 is 2, phase Neighbour salvages drive rod 16-6-3 and rotates coaxially connection；The salvaging crankshaft 16-6-5 is located at floater dragging device 16-6 bracket Lower part is salvaged crankshaft 16-6-5 and is connect by fixed hinge with marine salvage equipment 16-6 bracket, and the quantity for salvaging crankshaft 16-6-5 is 2 A, parallel and horizontal distance is 40cm~60cm between adjacent salvaging crankshaft 16-6-5；Described one end for salvaging the 16-6-4 that cranks arm It is rotatablely connected with crankshaft 16-6-5 is salvaged, it is 11 that every side, which salvages and salvages the quantity for the 16-6-4 that cranks arm on crankshaft 16-6-5,；It is described It salvages drive rod 16-6-3 and salvages 16-6-4 rotation of cranking arm by salvaging crankshaft 16-6-5 drive；The salvaging 16-6-4 that cranks arm is every Connection is fixed by the bracket between two, and the adjacent salvaging salvaged on crankshaft 16-6-5 cranks arm 16-6-4 by salvaging steel wire 16-6-7 connection；The steel wire slack adjuster 16-6-6 is located at four endpoints of floater dragging device 16-6 bracket, steel The quantity of silk slack adjuster 16-6-6 is 4, and steel wire slack adjuster 16-6-6 is connect with steel wire 16-6-7 is salvaged.
Further, this section is the explanation to heretofore described steel wire slack adjuster 16-6-6 structure.The steel Silk slack adjuster 16-6-6 includes: steel wire guide wheel 16-6-6-1, salvages steel wire 16-6-6-2, regulating device cooling system 16-6-6-3, regulating device motor 16-6-6-4, regulating device clutch 16-6-6-5；Steel wire guide wheel 16-6-6-1 In the entire middle and lower part steel wire slack adjuster 16-6-6, wherein salvaging steel wire 16-6-6-2 under steel wire guide wheel 16-6-6-1 Portion center penetrates, and is wrapped in steel wire hoop, and steel wire guide wheel 16-6-6-1 axis top is successively arranged regulating device cooling system System 16-6-6-3, regulating device motor 16-6-6-4 and regulating device clutch 16-6-6-5, steel wire guide wheel 16-6-6-1 are The hollow structure of bottom end opening；The regulating device cooling system 16-6-6-3 and steel wire guide wheel 16-6-6-1 axis upper end turn It is dynamic to connect, it is 5cm~10cm at a distance from the bottom regulating device cooling system 16-6-6-3 and steel wire guide wheel 16-6-6-1；It is described Regulating device motor 16-6-6-4 is fixedly connected with steel wire guide wheel 16-6-6-1 axis, the top regulating device motor 16-6-6-4 It is connect with regulating device clutch 16-6-6-5, regulating device motor 16-6-6-4 is controlled by conducting wire and Central Control Center 7 Connection；The regulating device clutch 16-6-6-5 is located at the top of entire steel wire slack adjuster 16-6-6；The steel wire Hoop is fixedly connected with steel wire guide wheel 16-6-6-1 axis.
Further, this section is saying to heretofore described integrated apparatus sedimentation basin secondary treatment system 16-8 structure It is bright.The integrated apparatus sedimentation basin secondary treatment system 16-8 includes: secondary sediment delivery pipe 16-8-1, secondary sediment storage Case 16-8-2, U-tube 16-8-3, secondary treatment system outlet pipe 16-8-4, dredge 16-8-5, secondary treatment system water inlet pipe 16-8-6；The dredge 16-8-5 waist upper end is equipped with secondary treatment system water inlet pipe 16-8-6, dredge 16-8-5 and two Secondary processing system water inlet pipe 16-8-6 is vertically through the tubule and mono- end cap of U-tube 16-8-3 of the one end dredge 16-8-5 lower part It connects, dredge 16-8-5 is arranged horizontally by tubule and U-tube 16-8-3 vertically through, dredge 16-8-5 and closed at both ends Cylindrical hollow structure；The bottom the U-tube 16-8-3 is equipped with secondary sediment hutch 16-8-2 and the two perforation connection, U The type pipe 16-8-3 other end and the seamless perforation of secondary treatment system outlet pipe 16-8-4；The secondary sediment hutch 16-8-2's Bottom and secondary sediment delivery pipe 16-8-1 perforation connect, and secondary sediment hutch 16-8-2 is the hollow of diameter 10cm~15cm Sphere structure.
Further, this section is the explanation to heretofore described dredge 16-8-5 structure.The dredge 16-8-5 It include: dredge mud mouth 16-8-5-1, dredge cavity 16-8-5-2, dredge piston 16-8-5-3, dredge water inlet 16-8-5-4, mandril top receiving apparatus 16-8-5-5, dredge mandril 16-8-5-6, dredge water outlet 16-8-5-7；It is described to dredge Logical device mandril 16-8-5-6 is located inside dredge 16-8-5, one end of dredge mandril 16-8-5-6 and mandril top receiving apparatus The other end of 16-8-5-5 connection, dredge mandril 16-8-5-6 is connect with dredge piston 16-8-5-3；It receives on the mandril top Device 16-8-5-5 is located at the one end entire dredge 16-8-5, and mandril top receiving apparatus 16-8-5-5 and dredge 16-8-5 is fixed Connection；The diameter of the dredge piston 16-8-5-3 is less than the diameter of dredge cavity 16-8-5-2；The dredge water inlet Mouth 16-8-5-4 is located at mono- upper lateral part of dredge 16-8-5, and dredge water inlet 16-8-5-4 and dredge cavity 16-8-5-2 hang down Straight perforation；The dredge water outlet 16-8-5-7 is located at another side lower part of dredge 16-8-5, dredge water outlet 16-8-5- 7 and dredge cavity 16-8-5-2 is vertically through the dredge bottom end water outlet 16-8-5-7 is equipped with valve；The dredge mud extraction Mouth 16-8-5-1 is located at the dredge side cavity 16-8-5-2 and the seamless perforation of the two, and the outer end dredge mud mouth 16-8-5-1 is set There is valve.
Further, this section is the explanation to heretofore described dredge piston 16-8-5-3 structure.The dredge Piston 16-8-5-3 includes: piston cylinder ring 16-8-5-3-1, dredge air outlet 16-8-5-3-2, piston pushing tow bolt 16-8-5- 3-3, dredge inner blower 16-8-5-3-4, dredge air inlet 16-8-5-3-5；The dredge air inlet 16-8-5-3-5 Positioned at entire dredge piston 16-8-5-3 device one end, dredge air inlet 16-8-5-3-5 and dredge mandril 16-8-5-6 Outer wall is penetrated through by bracket to be connected and forms channel；The dredge inner blower 16-8-5-3-4 is set to entire dredge piston Inside 16-8-5-3 device, the quantity of dredge inner blower 16-8-5-3-4 is 2, adjacent dredge inner blower 16-8-5-3-4 By rotating axis connection；The dredge air outlet 16-8-5-3-2 between adjacent dredge inner blower 16-8-5-3-4, And it is penetrated through before and after dredge air inlet 16-8-5-3-5 and dredge air outlet 16-8-5-3-2, dredge air outlet 16-8-5- The quantity of 3-2 is 4, and adjacent dredge air outlet 16-8-5-3-2 is isodistantly spaced distribution；The piston cylinder ring 16-8-5-3-1 It is fixedly connected on entire dredge piston 16-8-5-3 device outer wall surface, the quantity of piston cylinder ring 16-8-5-3-1 is no less than 2 A, the diameter of piston cylinder ring 16-8-5-3-1 is 5cm~10cm；The piston pushing tow bolt 16-8-5-3-3 is located at entire dredge The piston 16-8-5-3 device other end and the two is fixedly connected.
Further, the invention also discloses a kind of work sides of inexpensive integrated treatment high concentrated organic wastewater device Method, this method including the following steps:
Step 1: in a kind of inexpensive integrated treatment high concentrated organic wastewater device operation process, the sewage that is introduced from outside into Sewage inlet pipe 10 is flowed under the action of integrated apparatus surge tank 1；Meanwhile sewage pump 2 is in the control of Central Control Center 7 Under operated, the sewage in sewage inlet pipe 10 is sent to level-one anaerobic pond 13 and second level anoxic pond 14；Then, one is flowed into The sewage of grade anaerobic pond 13 enters level-one anoxic pond 11 by pipeline, and is flowed to respectively by pipelines different in level-one anoxic pond 11 Level-one aerobic tank 12 and secondary anaerobic pond 15；Sewage in level-one aerobic tank 12 and secondary anaerobic pond 15 passes through respective inside again Pipeline flows into second level anoxic pond 14, and successively flows into second level aerobic tank 17 and integrated apparatus sedimentation basin by second level anoxic pond 14 16；By the effect of integrated apparatus sedimentation basin 16, the sedimentation basin of sludge in sewage from 16 lower section of integrated apparatus sedimentation basin Sludge pipe 5 separately flows into outer sludge-discharge pipe 3 and reflux sludge tube 8；At the same time, the water for removing sludge flows into integrated apparatus filter Pond 18；The mud of the outer sludge-discharge pipe 3 of inflow is under the action of sludge water filter 4 outside discharger；Flow into reflux sludge tube 8 Sludge enters level-one anaerobic pond 13 and level-one anoxic pond 11 under the action of return sludge pump 6；Flow into integrated apparatus filter tank 18 Water by filtering after, entered after sterilization pool 19 carries out disinfection by pipeline and be discharged；Sewage is become reconciled in anaerobic ponds at different levels, anoxic pond In pond correlated response occurs for oxygen；
Step 2: in the operation of integrated apparatus sedimentation basin 16, waste water is entered clear by integrated apparatus sedimentation basin water inlet pipe 16-7 Water chamber 16-5；Under the action of floater dragging device 16-6, the floating material in waste water is picked up；Meanwhile the solid in waste water Object is settled down to tapered bed mud collecting tank 16-3 and is discharged from bed mud delivery pipe 16-1, and then remaining clear water is from integrated apparatus It is flowed out in sedimentation basin secondary treatment system 16-8；
Step 3: in floater dragging device jacking system 16-2 operation, lifting air pump 16-2-1 starts to transport after being powered up Make, subsequent gas is persistently delivered to high-pressure chamber 16-2-4 by air flue 16-2-3, and then forms air pressure；In the effect of air pressure Under, piston 16-2-5 pushes elevating lever 16-2-6 to move down；When piston 16-2-5 drops to the high-pressure chamber bottom 16-2-4, high pressure Chamber 16-2-4 and limit for height air valve 16-2-7 forms airflow channel, and high pressure gas is discharged by limit for height air valve 16-2-7, piston 16- 2-5 and elevating lever 16-2-6 are moved up；
Step 4: in limit for height air valve 16-2-7 operation, pressure sensor 16-2-7-2 monitors inner plenum 16-2-7-8 pressure in real time Power variation, when monitoring that right side inner plenum 16-2-7-8 pressure is more than setting value, Central Control Center 7 is by closing valve control Line packet 16-2-7-6, control close valve axis 16-2-7-7 and move right, and then drive air valve to close valve 16-2-7-5 and move to right, real Existing air valve, which closes valve 16-2-7-5, to be opened, and pressure release is carried out；When monitor right side inner plenum 16-2-7-8 pressure be less than setting value, Central Control Center 7 is by closing valve control line packet 16-2-7-6, and control is closed valve axis 16-2-7-7 and is moved to the left, and then band Valve of taking offence closes valve 16-2-7-5 and moves to left, and realizes that air valve closes valve 16-2-7-5 closure, right side inner plenum 16-2-7-8 pressure It gradually rises；
Step 5, clean water chamber 16-5 operation in, after sewage enters clean water chamber 16-5, pass sequentially through aerofoil profile dispersion plate 16-5-2, The gentle drop net 16-5-4 of rectangular slow drop plate 16-5-3, and slow drop of the realization to sewage under the synergy of three；COD sensor 16-5-5 is measured in real time the sewage for entering clean water chamber 16-5, when the concentration of sewage is more than normal concentration, COD sensor Warning message is sent to Central Control Center 7 by conducting wire by 16-5-5；When the sewage for entering clean water chamber 16-5 is more than in height In limited time, sewage flows into bed mud delivery pipe 16-1 from overflow port 16-5-6；
Step 6: it in floater dragging device 16-6 operation, after salvaging motor 16-6-1 powers on, drives and salvages cam 16- 6-2 is operated, and then drives the rotation salvaged drive rod 16-6-3 and salvage crankshaft 16-6-5, and by salvaging crankshaft 16- 6-5 drives downside to salvage swinging up and down for the 16-6-4 that cranks arm, and then realizes the salvaging to floating material；
Step 7: in steel wire slack adjuster 16-6-6 operation, steel wire 16-6-6-2 is salvaged from steel wire guide wheel 16-6-6-1 Bottom centre enters and is around in steel wire hoop；When regulating device motor 16-6-6-4, which powers on, to be operated, pass through adjusting Device clutch 16-6-6-5 drives steel wire hoop to implement the winding to steel wire 16-6-6-2 is salvaged；At the same time, regulating device is cold But system 16-6-6-3 cools to the steel wire slack adjuster 16-6-6 implementation of operating；
Step 8: in integrated apparatus sedimentation basin secondary treatment system 16-8 operation, sewage passes through secondary treatment system water inlet pipe 16-8-6 enters dredge 16-8-5, and then flows into U-tube 16-8-3 by dredge 16-8-5；Solid content in sewage is from U-shaped After the bottom pipe 16-8-3 enters secondary sediment hutch 16-8-2, sewage is discharged by secondary treatment system outlet pipe 16-8-4；Into The solid content for entering secondary sediment hutch 16-8-2 is discharged from secondary sediment delivery pipe 16-8-1；
Step 9: in dredge 16-8-5 operation, pending water enters dredge cavity by dredge water inlet 16-8-5-4 16-8-5-2, and be discharged from dredge water outlet 16-8-5-7；When mud is more in water, on dredge water outlet 16-8-5-7 The valve at end is closed, while dredge mandril 16-8-5-6 pushes piston forward under the action of the receiving apparatus 16-8-5-5 of mandril top It is mobile, and then mud is pushed to be discharged from dredge mud mouth 16-8-5-1；After dredging work, dredge water outlet The valve opening of the upper end 16-8-5-7, while dredge mandril 16-8-5-6 band under the action of the receiving apparatus 16-8-5-5 of mandril top Piston moves back reset, and then water is discharged from dredge water outlet 16-8-5-7；
Step 10: in dredge piston 16-8-5-3 operation, wind enters dredge from dredge air inlet 16-8-5-3-5 and lives It fills in inside 16-8-5-3, and to entire dredge piston 16-8-5-3 device under the action of dredge inner blower 16-8-5-3-4 It radiates；Radiation air is discharged from dredge air outlet 16-8-5-3-2.
A kind of low cost integrated treatment high concentrated organic wastewater device disclosed in the invention patent, the advantage is that: should Apparatus structure is rationally compact, and wastewater treatment efficiency is good, and cost is relatively low；The device piston is prepared using high molecular material, is mixed Conjunction speed enhancing rate is high, high efficiency, and the scope of application is wide.
Detailed description of the invention
Fig. 1 is a kind of heretofore described inexpensive integrated treatment high concentrated organic wastewater apparatus structure schematic diagram.
Fig. 2 is heretofore described 16 structural schematic diagram of integrated apparatus sedimentation basin.
Fig. 3 is heretofore described floater dragging device jacking system 16-2 structural schematic diagram.
Fig. 4 is heretofore described limit for height air valve 16-2-7 structural schematic diagram.
Fig. 5 is heretofore described clean water chamber 16-5 structural schematic diagram.
Fig. 6 is heretofore described floater dragging device 16-6 structural schematic diagram.
Fig. 7 is heretofore described steel wire slack adjuster 16-6-6 structural schematic diagram.
Fig. 8 is heretofore described integrated apparatus sedimentation basin secondary treatment system 16-8 structural schematic diagram.
Fig. 9 is heretofore described dredge 16-8-5 structural schematic diagram.
Figure 10 is heretofore described dredge piston 16-8-5-3 structural schematic diagram.
Figure 11 is O- ethyl O- (4- methyl mercapto phenyl) S- propyl disulfide substituted phosphate accounting to wear-resistant effect promoting rate Influence relational graph.
Specific embodiment
With reference to the accompanying drawings and examples to a kind of inexpensive integrated treatment high concentrated organic wastewater provided by the invention Device is further described.
As shown in Figure 1, being a kind of heretofore described inexpensive integrated treatment high concentrated organic wastewater apparatus structure Schematic diagram.As seen from the figure, comprising: integrated apparatus surge tank 1, sewage pump 2, outer sludge-discharge pipe 3, sludge water filter 4 sink Shallow lake pond sludge pipe 5, return sludge pump 6, Central Control Center 7, reflux sludge tube 8, integrated apparatus bracket 9, sewage inlet pipe 10, level-one anoxic pond 11, level-one aerobic tank 12, level-one anaerobic pond 13, second level anoxic pond 14, secondary anaerobic pond 15, one makeup Set sedimentation basin 16, second level aerobic tank 17, integrated apparatus filter tank 18, sterilization pool 19；The integrated apparatus bracket 9 is by 8 shapes Shape column of the same size connects and composes and is respectively formed the two slot rooms in left and right, and left side groove chamber interior is successively arranged level-one anaerobic pond 13, level-one anoxic pond 11, level-one aerobic tank 12, second level anoxic pond 14 and secondary anaerobic pond 15, right side groove chamber interior are successively arranged Second level aerobic tank 17, integrated apparatus sedimentation basin 16, integrated apparatus filter tank 18 and sterilization pool 19；The level-one anaerobic pond 13 with The level-one anoxic pond 11 of one side is penetrated through by pipeline and is connected, the right side of level-one anaerobic pond 13 and the fixed company of second level anoxic pond 14 It connects；The level-one anoxic pond 11 is passed through with the level-one aerobic tank 12 of one side, right side secondary anaerobic pond 15 respectively by different pipelines Lead to and connects；The level-one aerobic tank 12 is connected by pipeline and the perforation of second level anoxic pond 14；The second level aerobic tank 17 is located at one 9 right side groove room upper left side of body appliance stand, 17 side of second level aerobic tank are respectively equipped with integrated apparatus sedimentation basin 16 and one Filter tank 18 is set in makeup, and second level aerobic tank 17 is passed through with second level anoxic pond 14 and integrated apparatus sedimentation basin 16 respectively by different pipelines Lead to and connects；The integrated apparatus sedimentation basin 16, which is penetrated through with integrated apparatus filter tank 18 by pipeline, to be connected；The sterilization pool 19 It is arranged in 9 right side groove room right end of integrated apparatus bracket, sterilization pool 19 and integrated apparatus filter tank 18 and connection is penetrated through by pipeline； One end perforation of the sludge from sedimentation tank pipe 5 is connected to 16 lower section of integrated apparatus sedimentation basin, the other end of sludge from sedimentation tank pipe 5 Port is connected with reflux sludge tube 8 and the perforation of outer sludge-discharge pipe 3 respectively；Described 8 one end of reflux sludge tube respectively with level-one anaerobism Pond 13, the perforation connection of level-one anoxic pond 11, reflux sludge tube 8 are connected by return sludge pump 6 and the perforation of sludge from sedimentation tank pipe 5； The return sludge pump 6 is connected by conducting wire with the control of Central Control Center 7；The sludge water filter 4 is set to outlet sludge 3 front end of pipe, sludge water filter 4 and outer sludge-discharge pipe 3 penetrate through；The sewage inlet pipe 10 is set to outside integrated apparatus bracket 9 On the upside of portion, 10 one end of sewage inlet pipe is connected with level-one anaerobic pond 13 and the perforation of second level anoxic pond 14 respectively, sewage inlet pipe 10 The other end is penetrated through by the integrated apparatus surge tank 1 on 9 right side of sewage pump 2 and integrated apparatus bracket and is connected；The sewage pump 2 It is connect with Central Control Center 7 by polygon control survey.
As shown in Fig. 2, being heretofore described 16 structural schematic diagram of integrated apparatus sedimentation basin.As seen from the figure, one It includes: bed mud delivery pipe 16-1, floater dragging device jacking system 16-2, tapered bed mud collecting tank that sedimentation basin 16 is set in body makeup 16-3, integrated apparatus sedimentation basin bracket 16-4, clean water chamber 16-5, floater dragging device 16-6, integrated apparatus sedimentation basin Water inlet pipe 16-7, integrated apparatus sedimentation basin secondary treatment system 16-8；It is characterized in that, the integrated apparatus sedimentation basin branch Floater dragging device 16-6 and clean water chamber 16-5 is equipped with inside frame 16-4, and floater dragging device 16-6 is located at clean water chamber The top 16-5, integrated apparatus sedimentation basin bracket 16-4 are fixedly connected with clean water chamber 16-5, integrated apparatus sedimentation basin bracket 16- 4 quantity is 4, parallel between adjacent integrated apparatus sedimentation basin bracket 16-4 and be fixedly connected by horizontal truss；It is described Floater dragging device jacking system 16-2 is located at integrated apparatus sedimentation basin bracket 16-4 inner wall upper end and the two is fixedly connected, The floater dragging device side jacking system 16-2 is slidably connected with floater dragging device 16-6；The bottom of the clean water chamber 16-5 Portion is equipped with tapered bed mud collecting tank 16-3, and clean water chamber 16-5 and tapered bed mud collecting tank 16-3 surrounding seamless welding simultaneously penetrate through, clearly The side of water chamber 16-5 and integrated apparatus sedimentation basin secondary treatment system 16-8 are penetrated through, and clean water chamber 16-5 is hollow cuboid Structure；The lower end of the tapered bed mud collecting tank 16-3 is disposed with bed mud delivery pipe 16-1, and the two penetrates through；The one makeup It sets sedimentation basin water inlet pipe 16-7 and is located at 16 top of integrated apparatus sedimentation basin.
As shown in figure 3, being heretofore described floater dragging device jacking system 16-2 structural schematic diagram.From figure Find out, floater dragging device jacking system 16-2 includes: lifting air pump 16-2-1, gas bleeder valve 16-2-2, air flue 16-2-3, high Press chamber 16-2-4, piston 16-2-5, elevating lever 16-2-6, limit for height air valve 16-2-7；The gas bleeder valve 16-2-2 is located at lifting Between air pump 16-2-1 and air flue 16-2-3, the one end gas bleeder valve 16-2-2 and lifting air pump 16-2-1 perforation are connected, gas bleeder valve 16- The 2-2 other end and air flue 16-2-3 perforation connect；The lifting air pump 16-2-1 is connect by conducting wire with Central Control Center 7； The other end of the air flue 16-2-3 and the seamless perforation of high-pressure chamber 16-2-4；Piston is equipped with inside the high-pressure chamber 16-2-4 16-2-5 and elevating lever 16-2-6, high-pressure chamber's 16-2-4 outer wall lower end are equipped with limit for height air valve 16-2-7, high-pressure chamber 16-2-4 For hollow cylindrical structure；The piston 16-2-5 is slidably connected with high-pressure chamber's 16-2-4 inner wall, and piston 16-2-5's is straight Diameter is 3cm~5cm；The elevating lever 16-2-6 is located at piston lower portion and the two connects, and the diameter of elevating lever 16-2-6 is less than height Press the diameter of chamber 16-2-4；The limit for height air valve 16-2-7 and high-pressure chamber 16-2-4 perforation connects.
As shown in figure 4, being heretofore described limit for height air valve 16-2-7 structural schematic diagram.As seen from the figure, the limit High air valve 16-2-7 includes: limit for height valve manhole appendix 16-2-7-1, pressure sensor 16-2-7-2, limit for height valve air flue 16-2-7-3, Limit for height valve air inlet 16-2-7-4, air valve close valve 16-2-7-5, close valve control line packet 16-2-7-6, close valve axis 16- 2-7-7, inner plenum 16-2-7-8；The limit for height valve manhole appendix 16-2-7-1 and limit for height valve air inlet 16-2-7-4 are located at The both ends limit for height air valve 16-2-7, limit for height valve manhole appendix 16-2-7-1 and limit for height valve air inlet 16-2-7-4 pass through limit for height valve air flue 16-2-7-3 is mutually communicated；Inner plenum 16-2-7-8 is equipped with inside limit for height air valve 16-2-7；In inner plenum 16-2-7-8 Middle part, which is equipped with, closes valve control line packet 16-2-7-6, to close airtight structure, and inner plenum 16-2-7-8 is divided into Two independent inner plenum 16-2-7-8, two independent inner plenum 16-2-7-8 can only pass through limit for height valve air flue 16-2- 7-3 is just able to achieve perforation；It is equipped at the central axes the limit for height valve air flue 16-2-7-3 and closes valve axis 16-2-7-7, the two sliding Connection, pass valve axis 16-2-7-7 are electromagnetic structure, close the one end valve axis 16-2-7-7 and air valve closes valve 16-2-7-5 It is fixedly connected, when air valve pass, valve 16-2-7-5 is moved to close impermeable when left side is bonded with pass valve control line packet 16-2-7-6 Gas；The pressure sensor 16-2-7-2 is located at the side limit for height air valve 16-2-7, pressure sensor 16-2-7-2 by conducting wire with Central Control Center 7 connects；The pass valve control line packet 16-2-7-6 is connect by conducting wire with Central Control Center 7.
As shown in figure 5, being heretofore described clean water chamber 16-5 structural schematic diagram.As seen from the figure, clean water chamber 16-5 packet Include: clean water chamber frame 16-5-1, aerofoil profile dispersion plate 16-5-2, rectangular slow drop plate 16-5-3 delay drop net 16-5-4, COD sensor 16-5-5, overflow port 16-5-6；Aerofoil profile dispersion plate 16-5-2, rectangular slow drop plate are equipped with inside the clean water chamber frame 16-5-1 The gentle drop net 16-5-4 of 16-5-3；The clean water chamber frame 16-5-1 is hollow cylinder structure；The aerofoil profile dispersion plate 16-5-2 It is in different shaft staggered distributions, aerofoil profile dispersion plate 16-5-2 positioned at the rectangular slow drop top plate 16-5-3 and from rectangular slow drop plate 16-5-3 Quantity be 3, aerofoil profile dispersion plate 16-5-2 horizontal parallel arrangement and both ends be fixedly connected with the inner wall of clean water chamber 16-5, it is adjacent Aerofoil profile dispersion plate 16-5-2 is in be equally spaced；The slow drop net 16-5-4 is located at the rectangular slow drop lower part plate 16-5-3 and between the two Distance be 13cm~18cm；The quantity of the rectangular slow drop plate 16-5-3 is 4, rectangular slow drop plate 16-5-3 horizontal parallel row It arranges and both ends is fixedly connected with the inner wall of clean water chamber 16-5, for the slow drop plate 16-5-3 of adjacent prismatic in being equally spaced, adjacent prismatic is slow Dropping the distance between plate 16-5-3 is 5cm~10cm；The overflow port 16-5-6 is arranged in the upper end clean water chamber frame 16-5-1, overflows Head piece 16-5-6 is penetrated through by clean water chamber frame 16-5-1 and bed mud delivery pipe 16-1；The COD sensor 16-5-5 is arranged in Clean water chamber 16-5 inner wall side, COD sensor 16-5-5 are connected by conducting wire and the control of Central Control Center 7.
As shown in fig. 6, being heretofore described floater dragging device 16-6 structural schematic diagram.As seen from the figure, it floats Object marine salvage equipment 16-6 includes: to salvage motor 16-6-1, salvages cam 16-6-2, salvages drive rod 16-6-3, salvages the 16- that cranks arm 6-4 salvages crankshaft 16-6-5, steel wire slack adjuster 16-6-6, salvages steel wire 16-6-7；16-6-1, the salvaging motor It is fixedly connected in the upper end floater dragging device 16-6 and with mono- side stand of floater dragging device 16-6, salvages motor 16-6-1 One end be equipped with salvage cam 16-6-2, salvage motor 16-6-1 and salvage cam 16-6-2 transmission connection；The salvaging cam 16-6-2 periphery upper end, which is equipped with, salvages drive rod 16-6-3, salvages cam 16-6-2 and salvages one end of drive rod 16-6-3 not Connection is rotated coaxially, the diameter for salvaging cam 16-6-2 is 5cm~10cm；The quantity for salvaging drive rod 16-6-3 is 2, Adjacent salvaging drive rod 16-6-3 rotates coaxially connection；The salvaging crankshaft 16-6-5 is located at floater dragging device 16-6 bracket Lower part, salvage crankshaft 16-6-5 and connect with marine salvage equipment 16-6 bracket by fixed hinge, the quantity of salvaging crankshaft 16-6-5 It is 2, parallel and horizontal distance is 40cm~60cm between adjacent salvaging crankshaft 16-6-5；The salvaging cranks arm the one of 16-6-4 End is rotatablely connected with crankshaft 16-6-5 is salvaged, and it is 11 that every side, which salvages and salvages the quantity for the 16-6-4 that cranks arm on crankshaft 16-6-5,；Institute State salvage drive rod 16-6-3 by salvage crankshaft 16-6-5 drive salvage crank arm 16-6-4 rotation；It is described to salvage the 16-6-4 that cranks arm Connection is fixed by the bracket between every two, and the adjacent salvaging salvaged on crankshaft 16-6-5 cranks arm 16-6-4 by salvaging steel wire 16-6-7 connection；The steel wire slack adjuster 16-6-6 is located at four endpoints of floater dragging device 16-6 bracket, steel The quantity of silk slack adjuster 16-6-6 is 4, and steel wire slack adjuster 16-6-6 is connect with steel wire 16-6-7 is salvaged.
As shown in fig. 7, being heretofore described steel wire slack adjuster 16-6-6 structural schematic diagram.As seen from the figure, Steel wire slack adjuster 16-6-6 includes: steel wire guide wheel 16-6-6-1, salvages steel wire 16-6-6-2, regulating device cooling system Unite 16-6-6-3, regulating device motor 16-6-6-4, regulating device clutch 16-6-6-5；The steel wire guide wheel 16-6-6-1 Positioned at the entire middle and lower part steel wire slack adjuster 16-6-6, wherein salvaging steel wire 16-6-6-2 from steel wire guide wheel 16-6-6-1 Lower central penetrates, and is wrapped in steel wire hoop, and it is cooling that steel wire guide wheel 16-6-6-1 axis top is successively arranged regulating device System 16-6-6-3, regulating device motor 16-6-6-4 and regulating device clutch 16-6-6-5, steel wire guide wheel 16-6-6-1 For the hollow structure of bottom end opening；The regulating device cooling system 16-6-6-3 and steel wire guide wheel 16-6-6-1 axis upper end It is rotatablely connected, is 5cm~10cm at a distance from the bottom regulating device cooling system 16-6-6-3 and steel wire guide wheel 16-6-6-1；Institute It states regulating device motor 16-6-6-4 to be fixedly connected with steel wire guide wheel 16-6-6-1 axis, the top regulating device motor 16-6-6-4 End is connect with regulating device clutch 16-6-6-5, and regulating device motor 16-6-6-4 is controlled by conducting wire and Central Control Center 7 System connection；The regulating device clutch 16-6-6-5 is located at the top of entire steel wire slack adjuster 16-6-6；The steel Silk hoop is fixedly connected with steel wire guide wheel 16-6-6-1 axis.
As shown in figure 8, being heretofore described integrated apparatus sedimentation basin secondary treatment system 16-8 structural schematic diagram.From Find out in figure, integrated apparatus sedimentation basin secondary treatment system 16-8 includes: secondary sediment delivery pipe 16-8-1, secondary sediment storage Hide case 16-8-2, U-tube 16-8-3, secondary treatment system outlet pipe 16-8-4, dredge 16-8-5, secondary treatment system water inlet Pipe 16-8-6；The dredge 16-8-5 waist upper end be equipped with secondary treatment system water inlet pipe 16-8-6, dredge 16-8-5 with Secondary treatment system water inlet pipe 16-8-6 is vertically through the tubule of the one end dredge 16-8-5 lower part and the one end U-tube 16-8-3 Socket, dredge 16-8-5 is by tubule and U-tube 16-8-3 vertically through dredge 16-8-5 is arranged horizontally and two end seals The cylindrical hollow structure closed；The bottom the U-tube 16-8-3 is equipped with secondary sediment hutch 16-8-2 and the two perforation connection, The U-tube 16-8-3 other end and the seamless perforation of secondary treatment system outlet pipe 16-8-4；The secondary sediment hutch 16-8-2 Bottom and secondary sediment delivery pipe 16-8-1 perforation connect, secondary sediment hutch 16-8-2 be diameter 10cm~15cm in Empty sphere structure.
As shown in figure 9, being heretofore described dredge 16-8-5 structural schematic diagram.As seen from the figure, dredge 16-8- 5 include: dredge mud mouth 16-8-5-1, dredge cavity 16-8-5-2, dredge piston 16-8-5-3, dredge water inlet 16-8-5-4, mandril top receiving apparatus 16-8-5-5, dredge mandril 16-8-5-6, dredge water outlet 16-8-5-7；It is described to dredge Logical device mandril 16-8-5-6 is located inside dredge 16-8-5, one end of dredge mandril 16-8-5-6 and mandril top receiving apparatus The other end of 16-8-5-5 connection, dredge mandril 16-8-5-6 is connect with dredge piston 16-8-5-3；It receives on the mandril top Device 16-8-5-5 is located at the one end entire dredge 16-8-5, and mandril top receiving apparatus 16-8-5-5 and dredge 16-8-5 is fixed Connection；The diameter of the dredge piston 16-8-5-3 is less than the diameter of dredge cavity 16-8-5-2；The dredge water inlet Mouth 16-8-5-4 is located at mono- upper lateral part of dredge 16-8-5, and dredge water inlet 16-8-5-4 and dredge cavity 16-8-5-2 hang down Straight perforation；The dredge water outlet 16-8-5-7 is located at another side lower part of dredge 16-8-5, dredge water outlet 16-8-5- 7 and dredge cavity 16-8-5-2 is vertically through the dredge bottom end water outlet 16-8-5-7 is equipped with valve；The dredge mud extraction Mouth 16-8-5-1 is located at the dredge side cavity 16-8-5-2 and the seamless perforation of the two, and the outer end dredge mud mouth 16-8-5-1 is set There is valve.
It as shown in Figure 10, is heretofore described dredge piston 16-8-5-3 structural schematic diagram.As seen from the figure, it dredges Device piston 16-8-5-3 includes: piston cylinder ring 16-8-5-3-1, dredge air outlet 16-8-5-3-2, piston pushing tow bolt 16-8- 5-3-3, dredge inner blower 16-8-5-3-4, dredge air inlet 16-8-5-3-5；The dredge air inlet 16-8-5-3- 5 are located at entire dredge piston 16-8-5-3 device one end, dredge air inlet 16-8-5-3-5 and dredge mandril 16-8-5- 6 outer walls are penetrated through by bracket to be connected and forms channel；The dredge inner blower 16-8-5-3-4 is set to entire dredge piston Inside 16-8-5-3 device, the quantity of dredge inner blower 16-8-5-3-4 is 2, adjacent dredge inner blower 16-8-5-3-4 By rotating axis connection；The dredge air outlet 16-8-5-3-2 between adjacent dredge inner blower 16-8-5-3-4, And it is penetrated through before and after dredge air inlet 16-8-5-3-5 and dredge air outlet 16-8-5-3-2, dredge air outlet 16-8-5- The quantity of 3-2 is 4, and adjacent dredge air outlet 16-8-5-3-2 is isodistantly spaced distribution；The piston cylinder ring 16-8-5-3-1 It is fixedly connected on entire dredge piston 16-8-5-3 device outer wall surface, the quantity of piston cylinder ring 16-8-5-3-1 is no less than 2 A, the diameter of piston cylinder ring 16-8-5-3-1 is 5cm~10cm；The piston pushing tow bolt 16-8-5-3-3 is located at entire dredge The piston 16-8-5-3 device other end and the two is fixedly connected.
Following embodiment further illustrates the contents of the present invention, and as piston 16-2-5, it is significant components of the invention, Due to its presence, the service life of integral device is increased, it plays crucial work for the safety of integral device, even running With.For this purpose, by it is following be embodiment, further verify the component of the present invention, shown to be higher than other related The physical characteristic of patent.
Embodiment 1
Piston 16-2-5 of the present invention, and content meter by mass percentage are manufactured according to the following steps:
Step 1: the ultrapure water 22% that conductivity is 1.25 μ S/cm is added in a kettle, starts blender in reaction kettle, revolving speed For 125rpm, starts heat pump, reactor temperature is made to rise to 75 DEG C；Successively methylate ester derivative 30%, mixed aid It is 1%, to being completely dissolved, adjusting pH value is 5.5 for stirring, and thiophosphate analog derivative 25% is added, agitator speed is adjusted to 255rpm, temperature are 90 DEG C；
Step 2: O- ethyl O- (4- methyl mercapto phenyl) S- propyl disulfide substituted phosphate 15%~45%, (T-4)-bis- (diethyls is added Base aminodithioformic acid-S, S') zinc 2% be uniformly mixed；
Step 3: it is 1% that crosslinking agent, which is added, agitator speed 75rpm, and temperature is 90 DEG C, keeps this state 5 hours, discharges, enters Molding press can be prepared by piston 16-2-5.
Embodiment 2
Piston 16-2-5 of the present invention, and content meter by mass percentage are manufactured according to the following steps:
Step 1: the ultrapure water 32% that conductivity is 3.15 μ S/cm is added in a kettle, starts blender in reaction kettle, revolving speed For 375rpm, starts heat pump, reactor temperature is made to rise to 185 DEG C；Successively methylate ester derivative 65%, mixing helps Agent is 5%, and to being completely dissolved, adjusting pH value is 8.5 for stirring, thiophosphate analog derivative 60% is added, by agitator speed tune To 315rpm, temperature is 395 DEG C；
Step 2: O- ethyl O- (4- methyl mercapto phenyl) S- propyl disulfide substituted phosphate 45%, (T-4)-bis- (two sulphur of diethyl are added For carbamic acid-S, S') zinc 15% be uniformly mixed；
Step 3: it is 5% that crosslinking agent, which is added, agitator speed 235rpm, and temperature is 265 DEG C, keeps this state 25 hours, out Material, entering molding press can be prepared by piston 16-2-5.
Embodiment 3
Piston 16-2-5 of the present invention, and content meter by mass percentage are manufactured according to the following steps:
Step 1: the ultrapure water 29% that conductivity is 1.315 μ S/cm is added in a kettle, starts blender in reaction kettle, revolving speed For 178rpm, starts heat pump, reactor temperature is made to rise to 85 DEG C；Successively methylate ester derivative 39%, mixed aid It is 4%, to being completely dissolved, adjusting pH value is 5.8 for stirring, and thiophosphate analog derivative 40% is added, agitator speed is adjusted to 300rpm, temperature are 90 DEG C；
Step 2: O- ethyl O- (4- methyl mercapto phenyl) S- propyl disulfide substituted phosphate 40%, (T-4)-bis- (two sulphur of diethyl are added For carbamic acid-S, S') zinc 10% be uniformly mixed；
Step 3: it is 3% that crosslinking agent, which is added, agitator speed 90rpm, and temperature is 91 DEG C, keeps this state 8 hours, discharges, enters Molding press can be prepared by piston 16-2-5.
Reference examples
Reference examples are that the piston of certain commercially available brand is used for the service condition of piston operational process.
Embodiment 4
Piston described in piston 16-2-5 and reference examples that Examples 1 to 3 prepares is used for the use of piston operational process Situation compares, and unites using cubical expansivity, leak rate, with the viscous rate of cylinder body, compression ratio enhancing rate as technical indicator Meter, the results are shown in Table 1:
Table 1 is pair of the piston described in Examples 1 to 3 and reference examples for the parameters of the service condition of piston operational process Than as a result, as seen from Table 1, piston 16-2-5 of the present invention, cubical expansivity, leak rate, with the viscous rate of cylinder body, compression Than the product that enhancing rate is above prior art production.
In addition, being O- ethyl O- (4- methyl mercapto phenyl) S- propyl disulfide substituted phosphate accounting to wear-resistant as shown in figure 11 The influence relational graph of effect promoting rate.Find out in figure, as the important component of piston 16-2-5 material, incorporation produces raising Moral character can play the role of vital, mix its ingredient in terms of anti-wear effect enhancing rate substantially better than existing product.

Claims (10)

1. a kind of low cost integrated treatment high concentrated organic wastewater device, comprising: integrated apparatus surge tank (1), sewage pump (2), outer sludge-discharge pipe (3), sludge water filter (4), sludge from sedimentation tank pipe (5), return sludge pump (6), Central Control Center (7), reflux sludge tube (8), integrated apparatus bracket (9), sewage inlet pipe (10), level-one anoxic pond (11), level-one aerobic tank (12), level-one anaerobic pond (13), second level anoxic pond (14), secondary anaerobic pond (15), integrated apparatus sedimentation basin (16), second level are good Oxygen pond (17), integrated apparatus filter tank (18), sterilization pool (19)；It is characterized in that, the integrated apparatus bracket (9) is by 8 The consistent column of shape size connects and composes and is respectively formed the two slot rooms in left and right, and left side groove chamber interior is successively arranged level-one anaerobism Pond (13), level-one anoxic pond (11), level-one aerobic tank (12), second level anoxic pond (14) and secondary anaerobic pond (15), right side groove room Inside is successively arranged second level aerobic tank (17), integrated apparatus sedimentation basin (16), integrated apparatus filter tank (18) and sterilization pool (19)；The level-one anoxic pond (11) of the level-one anaerobic pond (13) and one side is penetrated through by pipeline and is connected, level-one anaerobic pond (13) right side is fixedly connected with second level anoxic pond (14)；The level-one anoxic pond (11) by different pipelines respectively with one side Level-one aerobic tank (12), right side secondary anaerobic pond (15) perforation connection；The level-one aerobic tank (12) passes through pipeline and second level Anoxic pond (14) perforation connection；The second level aerobic tank (17) is located at integrated apparatus bracket (9) right side groove room upper left side, second level Aerobic tank (17) side is respectively equipped with integrated apparatus sedimentation basin (16) and integrated apparatus filter tank (18), second level aerobic tank (17) It is connected respectively with second level anoxic pond (14) and integrated apparatus sedimentation basin (16) perforation by different pipelines；The integrated apparatus Sedimentation basin (16) and integrated apparatus filter tank (18) are penetrated through by pipeline to be connected；The sterilization pool (19) is arranged in integrated apparatus Bracket (9) right side groove room right end, sterilization pool (19) and integrated apparatus filter tank (18) are penetrated through by pipeline and are connected；The sedimentation basin One end perforation of sludge pipe (5) is connected to below integrated apparatus sedimentation basin (16), the other end port of sludge from sedimentation tank pipe (5) It is connected respectively with reflux sludge tube (8) and outer sludge-discharge pipe (3) perforation；Detest respectively with level-one described reflux sludge tube (8) one end Oxygen pond (13), level-one anoxic pond (11) perforation connection, reflux sludge tube (8) pass through return sludge pump (6) and sludge from sedimentation tank pipe (5) perforation connection；The return sludge pump (6) is connected by conducting wire with Central Control Center (7) control；The sludge water filtering Device (4) is set to outer sludge-discharge pipe (3) front end, and sludge water filter (4) and outer sludge-discharge pipe (3) penetrate through；The sewage inlet pipe (10) be set to integrated apparatus bracket (9) external upper, sewage inlet pipe (10) one end respectively with level-one anaerobic pond (13) and two Grade anoxic pond (14) penetrates through connection, and sewage inlet pipe (10) other end passes through on the right side of sewage pump (2) and integrated apparatus bracket (9) Integrated apparatus surge tank (1) penetrate through connection；The sewage pump (2) is connect with Central Control Center (7) by polygon control survey；
Floater dragging device jacking system (16-2) is equipped with inside integrated apparatus sedimentation basin (16)；
Limit for height air valve (16-2-7) is equipped with inside floater dragging device jacking system (16-2)；
The limit for height air valve (16-2-7) includes: limit for height valve manhole appendix (16-2-7-1), pressure sensor (16-2-7-2), limit for height Valve air flue (16-2-7-3), limit for height valve air inlet (16-2-7-4), air valve close valve (16-2-7-5), close valve control line packet (16-2-7-6) is closed valve axis (16-2-7-7), inner plenum (16-2-7-8)；The limit for height valve manhole appendix (16-2-7-1) Be located at the both ends limit for height air valve (16-2-7) with limit for height valve air inlet (16-2-7-4), limit for height valve manhole appendix (16-2-7-1) and Limit for height valve air inlet (16-2-7-4) is mutually communicated by limit for height valve air flue (16-2-7-3)；It is internal in limit for height air valve (16-2-7) Equipped with inner plenum (16-2-7-8)；It is equipped in the middle part of inner plenum (16-2-7-8) and closes valve control line packet (16-2-7-6), Inner plenum (16-2-7-8) is divided into two independent inner plenums (16-2-7-8) to close airtight structure by it, Two independent inner plenums (16-2-7-8) can only just be able to achieve perforation by limit for height valve air flue (16-2-7-3)；The limit for height It is equipped at the central axes valve air flue (16-2-7-3) and closes valve axis (16-2-7-7), the two is slidably connected, and closes valve axis (16- 2-7-7) it is electromagnetic structure, closes valve axis one end (16-2-7-7) and be fixedly connected with air valve pass valve (16-2-7-5), work as gas Valve pass valve (16-2-7-5) is moved to close airtight when left side is bonded with pass valve control line packet (16-2-7-6)；The pressure Sensor (16-2-7-2) is located at the side limit for height air valve (16-2-7), and pressure sensor (16-2-7-2) is controlled by conducting wire and center Center (7) connection processed；The pass valve control line packet (16-2-7-6) is connect by conducting wire with Central Control Center (7).
2. a kind of inexpensive integrated treatment high concentrated organic wastewater device according to claim 1, which is characterized in that institute Stating integrated apparatus sedimentation basin (16) includes: bed mud delivery pipe (16-1), and floater dragging device jacking system (16-2) is tapered Bed mud collecting tank (16-3), integrated apparatus sedimentation basin bracket (16-4), clean water chamber (16-5), floater dragging device (16- 6), integrated apparatus sedimentation basin water inlet pipe (16-7), integrated apparatus sedimentation basin secondary treatment system (16-8)；Its feature exists In, floater dragging device (16-6) and clean water chamber (16-5) are equipped with inside the integrated apparatus sedimentation basin bracket (16-4), And floater dragging device (16-6) is located at the top clean water chamber (16-5), integrated apparatus sedimentation basin bracket (16-4) and clean water chamber (16-5) is fixedly connected, and the quantity of integrated apparatus sedimentation basin bracket (16-4) is 4, adjacent integrated apparatus sedimentation basin bracket It is parallel and be fixedly connected by horizontal truss between (16-4)；The floater dragging device jacking system (16-2) is located at one Sedimentation basin bracket (16-4) inner wall upper end is set in makeup and the two is fixedly connected, the side floater dragging device jacking system (16-2) It is slidably connected with floater dragging device (16-6)；The bottom of the clean water chamber (16-5) is equipped with tapered bed mud collecting tank (16- 3), clean water chamber (16-5) and tapered bed mud collecting tank (16-3) surrounding seamless welding and penetrate through, the side of clean water chamber (16-5) with Integrated apparatus sedimentation basin secondary treatment system (16-8) perforation, clean water chamber (16-5) are hollow rectangular parallelepiped structure；The cone The lower end of type bed mud collecting tank (16-3) is disposed with bed mud delivery pipe (16-1), and the two penetrates through；The integrated apparatus precipitating Pond water inlet pipe (16-7) is located at integrated apparatus sedimentation basin (16) top.
3. a kind of inexpensive integrated treatment high concentrated organic wastewater device according to claim 2, which is characterized in that institute Stating floater dragging device jacking system (16-2) includes: lifting air pump (16-2-1), gas bleeder valve (16-2-2), air flue (16-2- 3), high-pressure chamber (16-2-4), piston (16-2-5), elevating lever (16-2-6), limit for height air valve (16-2-7)；The gas bleeder valve (16-2-2) is located between lifting air pump (16-2-1) and air flue (16-2-3), gas bleeder valve one end (16-2-2) and lifting air pump (16-2-1) perforation connection, gas bleeder valve (16-2-2) other end and air flue (16-2-3) perforation connect；Lifting air pump (the 16- 2-1) it is connect by conducting wire with Central Control Center (7)；The other end and high-pressure chamber (16-2-4) of the air flue (16-2-3) Seamless perforation；Piston (16-2-5) and elevating lever (16-2-6), high-pressure chamber are equipped with inside the high-pressure chamber (16-2-4) (16-2-4) outer wall lower end is equipped with limit for height air valve (16-2-7), and high-pressure chamber (16-2-4) is hollow cylindrical structure；It is described Piston (16-2-5) is slidably connected with high-pressure chamber (16-2-4) inner wall, and the diameter of piston (16-2-5) is 3cm~5cm；It is described Elevating lever (16-2-6) is located at piston lower portion and the two connects, and the diameter of elevating lever (16-2-6) is less than high-pressure chamber (16-2-4) Diameter；The limit for height air valve (16-2-7) and high-pressure chamber (16-2-4) perforation connect.
4. a kind of inexpensive integrated treatment high concentrated organic wastewater device according to claim 3, which is characterized in that institute Stating clean water chamber (16-5) includes: clean water chamber frame (16-5-1), aerofoil profile dispersion plate (16-5-2), rectangular slow drop plate (16-5-3), Slow drop net (16-5-4), COD sensor (16-5-5), overflow port (16-5-6)；It is set inside the clean water chamber frame (16-5-1) There is gentle drop net (16-5-4) of aerofoil profile dispersion plate (16-5-2), rectangular slow drop plate (16-5-3)；Clean water chamber frame (the 16-5- It 1) is hollow cylinder structure；The aerofoil profile dispersion plate (16-5-2) be located at the rectangular slow drop plate top (16-5-3) and with rectangular slow drop Plate (16-5-3) is 3 in different shaft staggered distributions, the quantity of aerofoil profile dispersion plate (16-5-2), aerofoil profile dispersion plate (16-5-2) water It puts down arranged in parallel and both ends to be fixedly connected with the inner wall of clean water chamber (16-5), adjacent aerofoil dispersion plate (16-5-2) is in equidistant point Cloth；The distance of slow drop net (16-5-4) positioned at the rectangular slow drop plate lower part (16-5-3) and between the two is 13cm~18cm； The quantity of rectangular slow drop plate (16-5-3) is 4, and rectangular slow drop plate (16-5-3) horizontal parallel arranges and both ends and clear water The inner wall of room (16-5) is fixedly connected, and for slow drop plate (16-5-3) of adjacent prismatic in being equally spaced, adjacent prismatic is slow to drop plate (16-5- It the distance between 3) is 5cm~10cm；The overflow port (16-5-6) is arranged in the upper end clean water chamber frame (16-5-1), overflow port (16-5-6) is penetrated through by clean water chamber frame (16-5-1) and bed mud delivery pipe (16-1)；COD sensor (16-5-5) cloth It is placed in clean water chamber (16-5) inner wall side, COD sensor (16-5-5) is connected by conducting wire and Central Control Center (7) control.
5. a kind of inexpensive integrated treatment high concentrated organic wastewater device according to claim 4, which is characterized in that institute Stating floater dragging device (16-6) includes: to salvage motor (16-6-1), is salvaged cam (16-6-2), and drive rod (16-6- is salvaged 3) it, salvages and cranks arm (16-6-4), salvage crankshaft (16-6-5), steel wire slack adjuster (16-6-6), salvage steel wire (16-6- 7)；The salvaging motor (16-6-1) be located at the floater dragging device upper end (16-6) and with floater dragging device (16-6) one Side stand is fixedly connected, salvage motor (16-6-1) one end be equipped with salvage cam (16-6-2), salvage motor (16-6-1) with Salvage cam (16-6-2) transmission connection；The salvaging cam (16-6-2) periphery upper end, which is equipped with, salvages drive rod (16-6- 3) it, salvages cam (16-6-2) not to be rotatablely connected coaxially with the one end for salvaging drive rod (16-6-3), salvage cam (16-6-2) Diameter be 5cm~10cm；The quantity for salvaging drive rod (16-6-3) is 2, and adjacent salvaging drive rod (16-6-3) is same Axis rotation connection；The lower part salvaged crankshaft (16-6-5) and be located at floater dragging device (16-6) bracket, salvages crankshaft (16-6-5) is connect by fixed hinge with marine salvage equipment (16-6) bracket, and the quantity for salvaging crankshaft (16-6-5) is 2, adjacent Salvaging parallel and horizontal distance between crankshaft (16-6-5) is 40cm~60cm；It is described salvaging crank arm (16-6-4) one end and beat Fish out crankshaft (16-6-5) rotation connection, it is 11 that every side, which salvages and salvages the quantity of (16-6-4) of cranking arm on crankshaft (16-6-5),；Institute State salvage drive rod (16-6-3) by salvage crankshaft (16-6-5) drive salvage crank arm (16-6-4) rotation；The salvaging is cranked arm Connection is fixed by the bracket between (16-6-4) every two, and (16-6-4) is cranked arm in the adjacent salvaging salvaged on crankshaft (16-6-5) By salvaging steel wire (16-6-7) connection；The steel wire slack adjuster (16-6-6) is located at floater dragging device (16-6) At four endpoints of bracket, the quantity of steel wire slack adjuster (16-6-6) is 4, steel wire slack adjuster (16-6-6) with Salvage steel wire (16-6-7) connection.
6. a kind of inexpensive integrated treatment high concentrated organic wastewater device according to claim 5, which is characterized in that institute Stating steel wire slack adjuster (16-6-6) includes: steel wire guide wheel (16-6-6-1), is salvaged steel wire (16-6-6-2), and dress is adjusted It sets cooling system (16-6-6-3), regulating device motor (16-6-6-4), regulating device clutch (16-6-6-5)；The steel wire Guide wheel (16-6-6-1) is located at entire steel wire slack adjuster (16-6-6) middle and lower part, wherein salvaging steel wire (16-6-6-2) It penetrates, and is wrapped in steel wire hoop from steel wire guide wheel (16-6-6-1) lower central, steel wire guide wheel (16-6-6-1) axis Top is successively arranged regulating device cooling system (16-6-6-3), regulating device motor (16-6-6-4) and regulating device clutch (16-6-6-5), steel wire guide wheel (16-6-6-1) are the hollow structure of bottom end opening；Regulating device cooling system (the 16- It 6-6-3) is rotatablely connected with steel wire guide wheel (16-6-6-1) axis upper end, regulating device cooling system (16-6-6-3) and steel wire The distance of the bottom guide wheel (16-6-6-1) is 5cm~10cm；The regulating device motor (16-6-6-4) and steel wire guide wheel (16-6-6-1) axis is fixedly connected, and the regulating device motor top (16-6-6-4) and regulating device clutch (16-6-6-5) are even It connects, regulating device motor (16-6-6-4) is connected by conducting wire and Central Control Center (7) control；The regulating device clutch (16-6-6-5) is located at the top of entire steel wire slack adjuster (16-6-6)；The steel wire hoop and steel wire guide wheel (16-6- 6-1) axis is fixedly connected.
7. a kind of inexpensive integrated treatment high concentrated organic wastewater device according to claim 6, which is characterized in that described Integrated apparatus sedimentation basin secondary treatment system (16-8) includes: secondary sediment delivery pipe (16-8-1), secondary sediment hutch (16-8-2), U-tube (16-8-3), secondary treatment system outlet pipe (16-8-4), dredge (16-8-5), secondary treatment system Water inlet pipe (16-8-6)；Dredge (16-8-5) the waist upper end is equipped with secondary treatment system water inlet pipe (16-8-6), dredging Device (16-8-5) and secondary treatment system water inlet pipe (16-8-6) vertically through, the tubule of one end lower part dredge (16-8-5) with The socket of U-tube one end (16-8-3), dredge (16-8-5) is by tubule and U-tube (16-8-3) vertically through dredge (16-8-5) is arranged horizontally and cylindrical hollow structure closed at both ends；The U-tube bottom (16-8-3) is equipped with secondary heavy Slag hutch (16-8-2) and the two perforation connection, U-tube (16-8-3) other end and secondary treatment system outlet pipe (16-8- 4) seamless perforation；The bottom of the secondary sediment hutch (16-8-2) and the perforation of secondary sediment delivery pipe (16-8-1) connect, Secondary sediment hutch (16-8-2) is the hollow-sphere structures of diameter 10cm~15cm.
8. a kind of inexpensive integrated treatment high concentrated organic wastewater device according to claim 7, which is characterized in that described Dredge (16-8-5) includes: dredge mud mouth (16-8-5-1), dredge cavity (16-8-5-2), dredge piston (16- 8-5-3), dredge water inlet (16-8-5-4), mandril top receiving apparatus (16-8-5-5), dredge mandril (16-8-5-6) are dredged Logical device water outlet (16-8-5-7)；The dredge mandril (16-8-5-6) is located at dredge (16-8-5) inside, dredge top One end of bar (16-8-5-6) is connect with mandril top receiving apparatus (16-8-5-5), the other end of dredge mandril (16-8-5-6) with Dredge piston (16-8-5-3) connection；Mandril top receiving apparatus (16-8-5-5) is located at entire dredge (16-8-5) one End, and mandril top receiving apparatus (16-8-5-5) is fixedly connected with dredge (16-8-5)；The dredge piston (16-8-5-3) Diameter be less than dredge cavity (16-8-5-2) diameter；The dredge water inlet (16-8-5-4) is located at dredge (16- A 8-5) upper lateral part, dredge water inlet (16-8-5-4) and dredge cavity (16-8-5-2) vertically through；The dredge Water outlet (16-8-5-7) is located at dredge (16-8-5) another side lower part, dredge water outlet (16-8-5-7) and dredge chamber Body (16-8-5-2) is vertically through the dredge water outlet bottom end (16-8-5-7) is equipped with valve；Dredge mud mouth (the 16- 8-5-1) it is located at the dredge cavity side (16-8-5-2) and the seamless perforation of the two, the outer end dredge mud mouth (16-8-5-1) is set There is valve.
9. a kind of inexpensive integrated treatment high concentrated organic wastewater device according to claim 8, which is characterized in that institute Stating dredge piston (16-8-5-3) includes: piston cylinder ring (16-8-5-3-1), dredge air outlet (16-8-5-3-2), piston Pushing tow bolt (16-8-5-3-3), dredge inner blower (16-8-5-3-4), dredge air inlet (16-8-5-3-5)；The dredging Device air inlet (16-8-5-3-5) is located at entire dredge piston (16-8-5-3) device one end, dredge air inlet (16-8-5- It 3-5) is penetrated through with dredge mandril (16-8-5-6) outer wall by bracket and connects and form channel；Dredge inner blower (the 16- It 8-5-3-4) is set to inside entire dredge piston (16-8-5-3) device, the quantity of dredge inner blower (16-8-5-3-4) is 2, adjacent dredge inner blower (16-8-5-3-4) passes through rotation axis connection；Dredge air outlet (16-8-5-3-2) position Between adjacent dredge inner blower (16-8-5-3-4), and dredge air inlet (16-8-5-3-5) and dredge air outlet Perforation before and after (16-8-5-3-2), the quantity of dredge air outlet (16-8-5-3-2) are 4, adjacent dredge air outlet (16- 8-5-3-2) it is isodistantly spaced distribution；The piston cylinder ring (16-8-5-3-1) is fixedly connected on entire dredge piston (16-8-5- 3) device outer wall surface, the quantity of piston cylinder ring (16-8-5-3-1) are no less than 2, the diameter of piston cylinder ring (16-8-5-3-1) For 5cm~10cm；The piston pushing tow bolt (16-8-5-3-3) is located at entire dredge piston (16-8-5-3) the device other end And the two is fixedly connected.
10. a kind of inexpensive integrated treatment high concentrated organic wastewater device according to claim 9, which is characterized in that should Device working method including the following steps:
Step 1: in a kind of inexpensive integrated treatment high concentrated organic wastewater device operation process, the sewage that is introduced from outside into Sewage inlet pipe (10) are flowed under the action of integrated apparatus surge tank (1)；Meanwhile sewage pump (2) is in Central Control Center (7) it is operated under control, the sewage in sewage inlet pipe (10) is sent to level-one anaerobic pond (13) and second level anoxic pond (14)；Then, the sewage for flowing into level-one anaerobic pond (13) is entered level-one anoxic pond (11) by pipeline, and passes through level-one anoxic pond (11) different pipelines flow to level-one aerobic tank (12) and secondary anaerobic pond (15) respectively in；Level-one aerobic tank (12) and secondary anaerobic Sewage in pond (15) passes through respective internal pipeline again and flows into second level anoxic pond (14), and is successively flowed by second level anoxic pond (14) Enter second level aerobic tank (17) and integrated apparatus sedimentation basin (16)；By the effect of integrated apparatus sedimentation basin (16), in sewage Sludge from the sludge from sedimentation tank pipe (5) below integrated apparatus sedimentation basin (16) separately flow into outer sludge-discharge pipe (3) and reflux Sludge pipe (8)；At the same time, the water for removing sludge flows into integrated apparatus filter tank (18)；Flow into the mud of outer sludge-discharge pipe (3) Under the action of sludge water filter (4) outside discharger；The sludge of reflux sludge tube (8) is flowed into return sludge pump (6) Effect is lower to enter level-one anaerobic pond (13) and level-one anoxic pond (11)；The water of integrated apparatus filter tank (18) is flowed by filtering Afterwards, entered after sterilization pool (19) carries out disinfection by pipeline and be discharged；Sewage is sent out in anaerobic ponds at different levels, anoxic pond and aerobic tank Raw correlated response；
Step 2: integrated apparatus sedimentation basin (16) operation in, waste water by integrated apparatus sedimentation basin water inlet pipe (16-7) into Enter clean water chamber (16-5)；Under the action of floater dragging device (16-6), the floating material in waste water is picked up；Meanwhile waste water In solid content be settled down to tapered bed mud collecting tank (16-3) and the discharge from the bed mud delivery pipe (16-1), and then remaining clear water From outflow in integrated apparatus sedimentation basin secondary treatment system (16-8)；
Step 3: in floater dragging device jacking system (16-2) operation, lifting air pump (16-2-1) is opened after being powered up Begin to operate, subsequent gas is persistently delivered to high-pressure chamber (16-2-4) by air flue (16-2-3), and then forms air pressure；In air pressure Under the action of, piston (16-2-5) pushes elevating lever (16-2-6) to move down；When piston (16-2-5) drops to high-pressure chamber (16- 2-4) when bottom, high-pressure chamber (16-2-4) and limit for height air valve (16-2-7) form airflow channel, and high pressure gas passes through limit for height gas Valve (16-2-7) discharge, piston (16-2-5) and elevating lever (16-2-6) move up；
Step 4: in limit for height air valve (16-2-7) operation, pressure sensor (16-2-7-2) monitors inner plenum (16-2- in real time 7-8) pressure change, when monitoring that right side inner plenum (16-2-7-8) pressure is more than setting value, Central Control Center (7) passes through It closes valve control line packet (16-2-7-6), control closes valve axis (16-2-7-7) and moves right, and then air valve is driven to close valve (16-2-7-5) is moved to right, and is realized that air valve closes valve (16-2-7-5) and opens, is carried out pressure release；When monitoring right side inner plenum (16- 2-7-8) pressure is less than setting value, and Central Control Center (7) by closing valve control line packet (16-2-7-6), close in valve by control Axis (16-2-7-7) is moved to the left, and then is driven air valve to close valve (16-2-7-5) and moved to left, and realizes that air valve closes valve (16-2-7- 5) it is closed, right side inner plenum (16-2-7-8) pressure gradually rises；
Step 5 after sewage enters clean water chamber (16-5), passes sequentially through aerofoil profile dispersion plate in clean water chamber (16-5) operation Gentle drop net (16-5-4) of (16-5-2), rectangular slow drop plate (16-5-3), and realize under the synergy of three to sewage Slow drop；COD sensor (16-5-5) is measured in real time the sewage for entering clean water chamber (16-5), when the concentration of sewage is more than rule When determining concentration, warning message is sent to Central Control Center (7) by conducting wire by COD sensor (16-5-5)；When enter clear water When the sewage of room (16-5) is more than upper height limit, sewage flows into bed mud delivery pipe (16-1) from overflow port (16-5-6)；
Step 6: in floater dragging device (16-6) operation, after salvaging motor (16-6-1) powers on, drive salvaging convex Wheel (16-6-2) is operated, and then drives the rotation salvaged drive rod (16-6-3) and salvage crankshaft (16-6-5), and pass through Salvaging crankshaft (16-6-5) drives downside to salvage the swinging up and down of (16-6-4) of cranking arm, and then realizes the salvaging to floating material；
Step 7: in steel wire slack adjuster (16-6-6) operation, steel wire (16-6-6-2) is salvaged from steel wire guide wheel (16- 6-6-1) bottom centre enters and is around in steel wire hoop；When regulating device motor (16-6-6-4), which powers on, to be operated, Steel wire hoop is driven to implement the winding to steel wire (16-6-6-2) is salvaged by regulating device clutch (16-6-6-5)；It is same with this When, regulating device cooling system (16-6-6-3) cools to steel wire slack adjuster (16-6-6) implementation of operating；
Step 8: in integrated apparatus sedimentation basin secondary treatment system (16-8) operation, sewage is intake by secondary treatment system It manages (16-8-6) and enters dredge (16-8-5), and then U-tube (16-8-3) is flowed by dredge (16-8-5)；Consolidating in sewage After shape object enters secondary sediment hutch (16-8-2) from the U-tube bottom (16-8-3), sewage is by secondary treatment system outlet pipe (16-8-4) discharge；Row in into the solid content of secondary sediment hutch (16-8-2) from secondary sediment delivery pipe (16-8-1) Out；
Step 9: in dredge (16-8-5) operation, pending water enters dredge by dredge water inlet (16-8-5-4) Cavity (16-8-5-2), and be discharged from dredge water outlet (16-8-5-7)；When mud is more in water, dredge water outlet The valve of the upper end (16-8-5-7) is closed, while dredge mandril (16-8-5-6) is in the work of mandril top receiving apparatus (16-8-5-5) It is moved forward with lower promotion piston, and then pushes mud discharge from dredge mud mouth (16-8-5-1)；When dredging work knot Shu Hou, the valve opening of the upper end dredge water outlet (16-8-5-7), while dredge mandril (16-8-5-6) are received on mandril top Band piston moves back reset under the action of device (16-8-5-5), and then makes water row from dredge water outlet (16-8-5-7) Out；
Step 10: in dredge piston (16-8-5-3) operation, wind enters from dredge air inlet (16-8-5-3-5) to be dredged Device piston (16-8-5-3) is internal, and to entire dredge piston (16- under the action of dredge inner blower (16-8-5-3-4) 8-5-3) device radiates；Radiation air discharge from dredge air outlet (16-8-5-3-2)；
The piston (16-2-5) is made of high molecular material, and content meter, constituent are as follows by mass percentage:
Methyl ester derivative 30%~65%, thiophosphate analog derivative 25%~60%, mixed aid are 1%~5%, crosslinking agent For 1%~5%, O- ethyl O- (4- methyl mercapto phenyl) S- propyl disulfide substituted phosphate 15%~45%, (T-4)-bis- (two sulphur of diethyl For carbamic acid-S, S') zinc 2%~15%；
The feature of the methyl ester derivative molecular structure are as follows:
Wherein R is the alkyl that carbon atom number is 1~8；
The feature of the group thiophosphate derivative molecular structure are as follows:
Its molecular formula: C10H15O3PS2；Molecular weight: 278.343；
The mixed aid is oxysilane substance, and molecular structural formula includes:
The molecular formula of its included molecular structure are as follows: C16H20O2Si；
The crosslinking agent is phosphordithiic acid diisopropyl ester sodium, isopentyl and isopropyl) phosphorodithioate zinc salt, tetraphenyl Any one in (bisphenol-A) bisphosphate；
The preparation method of piston (16-2-5) comprising the steps of:
Step 1: the ultrapure water 22%~32% that conductivity is 1.25 μ of μ S/cm~3.15 S/cm, starting reaction are added in a kettle Blender in kettle, revolving speed are 125rpm~375rpm, start heat pump, reactor temperature is made to rise to 75 DEG C~185 DEG C；According to Secondary methylate ester derivative 30%~65%, mixed aid are 1%~5%, stirring to being completely dissolved, adjust pH value be 5.5~ 8.5, thiophosphate analog derivative 25%~60% is added, agitator speed is adjusted to 255rpm~315rpm, temperature is 90 DEG C ~395 DEG C；
Step 2: O- ethyl O- (4- methyl mercapto phenyl) S- propyl disulfide substituted phosphate 15%~45%, (T-4)-bis- (diethyls is added Base aminodithioformic acid-S, S') zinc 2%~15% be uniformly mixed；
Step 3: it is 1~5% that crosslinking agent, which is added, and agitator speed is 75rpm~235rpm, and temperature is 90 DEG C~265 DEG C, is kept This state 5~25 hours, discharging, entering molding press can be prepared by piston (16-2-5).
CN201811170950.3A 2018-10-09 2018-10-09 A kind of low cost integrated treatment high concentrated organic wastewater device Withdrawn CN109293139A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110656677A (en) * 2019-08-23 2020-01-07 谢红日 Water inflow device is prevented blockking up in aquatic

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110656677A (en) * 2019-08-23 2020-01-07 谢红日 Water inflow device is prevented blockking up in aquatic

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Application publication date: 20190201