CN205575858U - Useless organics in water and heavy metal ion's equipment is handled to microwave fluidized bed - Google Patents

Useless organics in water and heavy metal ion's equipment is handled to microwave fluidized bed Download PDF

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Publication number
CN205575858U
CN205575858U CN201620401144.2U CN201620401144U CN205575858U CN 205575858 U CN205575858 U CN 205575858U CN 201620401144 U CN201620401144 U CN 201620401144U CN 205575858 U CN205575858 U CN 205575858U
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China
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water
organic
organic substance
equipment
heavy metal
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Expired - Fee Related
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CN201620401144.2U
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Chinese (zh)
Inventor
孙玉红
高向琪
高涵
王宁
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Jining University
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Jining University
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Abstract

The utility model discloses an useless organics in water and heavy metal ion's equipment is handled to microwave fluidized bed belongs to effluent treatment plant technical field, including retrieving the room organically, it is linked together with the evaporating chamber through waste water transfer passage to retrieve the room organically, being equipped with rather than communicating microwave heating equipment all around of evaporating chamber, the below of evaporating chamber is equipped with central tube, central tube's one end intercommunication evaporating chamber, the other end communicates to the inside of crystallization fluidized bed, the top of evaporating chamber is equipped with the air outlet channel rather than the one end intercommunication, air outlet channel's other end intercommunication condensing tower, exhalant canal intercommunication water storage device is passed through to the below of condensing tower, it detects the controller to be equipped with PH on the exhalant canal, can high -efficient organic matter and the heavy metal ion who retrieves in the waste water through this equipment, and guarantee to retrieve the cleanliness of water after accomplishing, and the secondary pollution is avoided. Thus, the operation efficiency is improved.

Description

Microwave fluidized bed processing is given up the equipment of Organic substance in water and heavy metal ion
Technical field
This utility model relates to a kind of microwave fluidized bed processing and gives up the equipment of Organic substance in water and heavy metal ion, belongs to waste water and processes Device technique field.
Background technology
Along with China industry fast development, heavy metal wastewater thereby quantum of output is increasing, these waste water essentially from mine drainage, Waste-rock yard leaching water, the mine tailing draining of ore dressing field, non-ferrous metals smelting works' draining, Non-ferrous Metals Processing Factory's pickling waste waters, Electroplate Factory The various industrial wastewaters such as plating piece washings, steel plant's pickling draining and electrolysis, pesticide, medicine, paint and dyestuff, above-mentioned waste water In in addition to containing heavy metal ion often possibly together with a small amount of Organic substance, the most efficiently process these heavy metals and organic useless Water is also allowed to resource, it has also become problem the most in the urgent need to address, and evaporation is the effective way processing heavy metal ion-containing waste water One of footpath, microwave heating is as a kind of novel heating means, and crystallization fluid bed refers to make heavy metal ion in fluidisation by medium Carry out the process growing and being dried under state, prior art uses heating surface area during microwave heating less, cause microwave heating Inefficiency, meanwhile, steam after evaporation, it cannot be guaranteed that cleannes are to reach the degree recycled, are emitted on the external world and make Become secondary pollution.
Utility model content
The purpose of this utility model is to provide a kind of microwave fluidized bed processing to give up the equipment of Organic substance in water and heavy metal ion, energy Organic substance in enough high efficiente callback waste water and heavy metal ion, and ensure to have reclaimed the cleannes of rear water resource, it is to avoid secondary is dirty Dye, improves work efficiency.
Microwave fluidized bed processing described in the utility model is given up the equipment of Organic substance in water and heavy metal ion, including organic recovery room, Organic recovery room is connected with vaporization chamber by waste water transfer passage, and the inside of organic recovery room is provided with several by being distributed up and down The Organic substance recovery area of filtering baffle composition, the Organic substance that is arranged over of each Organic substance recovery area concentrates mouth, Organic substance concentration mouth Side be provided with Organic substance concentrate groove, Organic substance concentrate groove outside be provided with the organic outlet communicated therewith, organic recovery room Inwall is provided with heater, and waste water transfer passage is respectively equipped with suction pump and surpasses in the position connecting organic recovery room and vaporization chamber Sonic nebulizers, waste water transfer passage extends to the position of evaporation chamber and is provided with shower nozzle, being formed around and its phase of vaporization chamber Logical microwave heating equipment, evaporation chamber be arranged over demister, the lower section of vaporization chamber is provided with central tube, central canal One end connection vaporization chamber in road, the other end is communicated to crystallize the inside of fluid bed, and crystallization fluid bed includes separation chamber and crystallisation chamber, Crystallisation chamber is positioned at the lower section of separation chamber, and the lower end of crystallisation chamber is provided with the source of the gas communicated therewith, and the side below crystallisation chamber is provided with solid Outlet, the top of vaporization chamber is provided with the outlet passageway connected with its one end, the other end connection condensing tower of outlet passageway, condensing tower Lower section by exhalant canal interconnected water storage device, exhalant canal is provided with PH and detects controller, is provided with backflow outside exhalant canal Passage, one end of return flow line connects exhalant canal by electromagnetic valve, and the other end connects with waste water transfer passage, and PH detects control Device electrical connection electromagnetic valve.
It is indoor that waste water initially enters organic recovery, and the waste water that organic recovery is indoor is heated by heater, and waste water is through dividing up and down Organic recovery indoor bending that acts on of the filtering baffle of cloth is flowed, and Organic substance enters Organic substance and concentrates at mouth, and through Organic substance Concentrate mouth to flow in Organic substance concentration groove, flowed in collection device by organic outlet, reclaim organic waste water by useless Water transfer passage is delivered in vaporization chamber, is atomized through soniclizer before entering vaporization chamber, sprays at shower nozzle To vaporization chamber, the waste water after atomization is heated by the microwave heating equipment in vaporization chamber, and the moisture in waste water is with steam Form flows out in outlet passageway, and the remaining saturated solution containing heavy metal ion enters in entering fluid crystal bed by central tube Row fluidized crystallization, accelerates crystallization by source of the gas toward ventilation in crystallisation chamber, and the solid after crystallization flows out through solid outlet, enters out The steam of gas passage flows out in exhalant canal after carrying out being condensed into aqueous water in initially entering condensing tower, the PH on exhalant canal The pH value of aqueous water is detected by detection controller, sets the numerical range of pH value in PH detection controller, if detect PH value is in the numerical range set, and aqueous water flows in water storage device, if the pH value detected is not at the numerical range set In, drive electromagnetic valve to open, aqueous water carries out evaporative filtration again in again flowing into waste water transfer passage by return flow line, with Guarantee has processed the cleannes of rear aqueous water.
The lower section of described organic recovery room is provided with sundry storage device, in the effect waste water of the filtering baffle being distributed up and down Impurity can be partitioned in sundry storage device.
Described microwave heating equipment includes at least 4, lays respectively at the left and right sides of vaporization chamber, improves the efficiency of microwave heating.
Described outlet passageway is provided with air exhauster, is drawn in outlet passageway by steam by air exhauster.
The outside of described organic recovery room is provided with the waterwater entrance communicated therewith, and makes waste water flow at waterwater entrance when putting into Machine reclaims indoor.
This utility model compared with prior art, has the advantages that
The equipment providing a kind of microwave fluidized bed processing to give up Organic substance in water and heavy metal ion, utilizes microwave heating and fluid bed skill Art can Organic substance in high efficiente callback waste water and heavy metal ion, increase heating surface area during microwave heating further, and ensure Reclaim the cleannes of rear water resource, it is to avoid secondary pollution, improved work efficiency, produced by fluid crystal bed simultaneously Crystal has the advantages that volume is big, granule is uniform, production capacity is big, reduces the labor intensity of workman.
Accompanying drawing explanation
Fig. 1 is the structural representation of this utility model embodiment;
In figure: 1, waterwater entrance;2, organic recovery room;3, suction pump;4, soniclizer;5, demister; 6, outlet passageway;7, air exhauster;8, condensing tower;9, PH detects controller;10, exhalant canal;11, electromagnetism Valve;12, water storage device;13, return flow line;14, solid outlet;15, central tube;16, crystallization fluid bed; 17, microwave heating equipment;18, vaporization chamber;19, waste water transfer passage;20, shower nozzle;21, source of the gas;22, foreign material Storage device;23, filtering baffle.
Detailed description of the invention
With embodiment, this utility model is further described below in conjunction with the accompanying drawings:
Embodiment
The equipment of Organic substance in water and heavy metal ion as it is shown in figure 1, microwave fluidized bed processing described in the utility model is given up, bag Including organic recovery room 2, organic recovery room 2 is connected with vaporization chamber 18 by waste water transfer passage 19, organic recovery room 2 Inside is provided with several Organic substance recovery areas being made up of the filtering baffle 23 being distributed up and down, and the top of each Organic substance recovery area sets Having Organic substance to concentrate mouth, Organic substance is concentrated the side of mouth to be provided with Organic substance and is concentrated groove, and Organic substance concentrates the outside of groove to be provided with and its phase Logical organic outlet, the inwall of organic recovery room 2 is provided with heater, and waste water transfer passage 19 is connecting organic recovery room 2 Being respectively equipped with suction pump 3 and soniclizer 4 with the position of vaporization chamber 18, waste water transfer passage 19 extends to vaporization chamber Position within 18 is provided with shower nozzle 20, the microwave heating equipment 17 being formed around communicating therewith of vaporization chamber 18, vaporization chamber 18 Internal is arranged over demister 5, and the lower section of vaporization chamber 18 is provided with central tube 15, and one end connection of central tube 15 is steamed Sending out room 18, the other end is communicated to crystallize the inside of fluid bed 16, and crystallization fluid bed 16 includes separation chamber and crystallisation chamber, crystallisation chamber Being positioned at the lower section of separation chamber, the lower end of crystallisation chamber is provided with the source of the gas 21 communicated therewith, and the side below crystallisation chamber is provided with solid outlet 14, the top of vaporization chamber 18 is provided with the outlet passageway 6 connected with its one end, the other end connection condensing tower 8 of outlet passageway 6, Exhalant canal 10 interconnected water storage device 12 is passed through in the lower section of condensing tower 8, and exhalant canal 10 is provided with PH and detects controller 9, goes out Aquaporin 10 is outside is provided with return flow line 13, and one end of return flow line 13 connects exhalant canal 10 by electromagnetic valve 11, another End connects with waste water transfer passage 19, and PH detection controller 9 is electrically connected electromagnetic valve 11.
In order to further illustrate above-described embodiment, the lower section of organic recovery room 2 is provided with sundry storage device 22.
In order to further illustrate above-described embodiment, microwave heating equipment 17 includes at least 4, lays respectively at a left side for vaporization chamber 18 Right both sides.
In order to further illustrate above-described embodiment, outlet passageway 6 is provided with air exhauster 7.
In order to further illustrate above-described embodiment, the outside of organic recovery room 2 is provided with the waterwater entrance 1 communicated therewith.
The operation principle of the present embodiment is: flowing in organic recovery room 2 by waste water by waterwater entrance 1, heater is to organic time The waste water received in room 2 heats, and waste water acts on bend flow in organic recovery room 2 through the filtering baffle 23 that is distributed up and down Dynamic, Organic substance enters Organic substance and concentrates at mouth, and in Organic substance concentrates mouth inflow Organic substance to concentrate groove, is gone out by Organic substance Mouth flows in collection device, and the impurity of waste water can be partitioned in sundry storage device 22, has reclaimed organic waste water by useless Water transfer passage 19 is delivered in vaporization chamber 18, is atomized through soniclizer 4 before entering vaporization chamber 18, from Being ejected at shower nozzle 20 in vaporization chamber 18, waste water therein is heated by the microwave heating equipment 17 in vaporization chamber 18, useless Moisture in water flows out in outlet passageway 6 as water vapor, and the remaining saturated solution containing heavy metal ion passes through center Pipeline 15 carries out fluidized crystallization in entering fluid crystal bed 16, accelerates crystallization, after crystallization by source of the gas 21 toward ventilation in crystallisation chamber Solid flow out through solid outlet 14, enter outlet passageway 6 steam initially enter condensing tower 8 in carry out being condensed into liquid Flowing out in exhalant canal 10 after water, the pH value of aqueous water is detected by the PH detection controller 9 on exhalant canal 10, The numerical range of pH value, if the pH value detected is in the numerical range set, liquid water stream is set in PH detection controller 9 Entering in water storage device 12, if the pH value detected is not in the numerical range set, drive electromagnetic valve 11 to open, aqueous water leads to Cross in return flow line 13 again flows into waste water transfer passage 19 and carry out evaporative filtration again, processed rear aqueous water with guarantee Cleannes.
The microwave fluidized bed processing of embodiment of the present utility model described above in association with accompanying drawing is used to give up Organic substance in water and heavy metal The equipment of ion, it is possible to the Organic substance in high efficiente callback waste water and heavy metal ion, and ensure to have reclaimed the cleaning of rear water resource Degree, it is to avoid secondary pollution, improves work efficiency.But this utility model is not limited to described embodiment, without departing from this Change that in the case of the principle of utility model and spirit, embodiment is carried out by these, revise, replace and deformation still falls within this reality With in novel protection domain.

Claims (5)

1. a microwave fluidized bed processing is given up the equipment of Organic substance in water and heavy metal ion, it is characterised in that: include organic recovery Room (2), organic recovery room (2) is connected with vaporization chamber (18) by waste water transfer passage (19), organic recovery room (2) Inside be provided with several Organic substance recovery areas being made up of the filtering baffle (23) being distributed up and down, each Organic substance recovery area Being arranged over Organic substance and concentrate mouth, Organic substance is concentrated the side of mouth to be provided with Organic substance and is concentrated groove, and Organic substance concentrates the outside of groove to be provided with The organic outlet communicated therewith, the inwall of organic recovery room (2) is provided with heater, and waste water transfer passage (19) is in connection The position of organic recovery room (2) and vaporization chamber (18) is respectively equipped with suction pump (3) and soniclizer (4), waste water The position that transfer passage (19) extends to vaporization chamber (18) internal is provided with shower nozzle (20), being formed around of vaporization chamber (18) The microwave heating equipment (17) communicated therewith, what vaporization chamber (18) was internal is arranged over demister (5), vaporization chamber (18) Lower section be provided with central tube (15), one end of central tube (15) connection vaporization chamber (18), the other end is communicated to crystallization stream Changing the inside of bed (16), crystallization fluid bed (16) includes separation chamber and crystallisation chamber, and crystallisation chamber is positioned at the lower section of separation chamber, knot The lower end of brilliant room is provided with the source of the gas (21) communicated therewith, and the side below crystallisation chamber is provided with solid outlet (14), vaporization chamber (18) Top be provided with the outlet passageway (6) connected with its one end, the other end of outlet passageway (6) connection condensing tower (8), condensing tower (8) exhalant canal (10) interconnected water storage device (12) is passed through in lower section, and exhalant canal (10) is provided with PH and detects controller (9), exhalant canal (10) is outside is provided with return flow line (13), and the one end of return flow line (13) is by electromagnetic valve (11) even Pass-out aquaporin (10), the other end connects with waste water transfer passage (19), PH detection controller (9) electrical connection electromagnetic valve (11)。
Microwave fluidized bed processing the most according to claim 1 is given up the equipment of Organic substance in water and heavy metal ion, and its feature exists In: the lower section of described organic recovery room (2) is provided with several sundry storage devices (22).
Microwave fluidized bed processing the most according to claim 1 is given up the equipment of Organic substance in water and heavy metal ion, and its feature exists In: described microwave heating equipment (17) includes at least 4, lays respectively at the left and right sides of vaporization chamber (18).
Microwave fluidized bed processing the most according to claim 1 is given up the equipment of Organic substance in water and heavy metal ion, and its feature exists In: described outlet passageway (6) is provided with air exhauster (7).
Microwave fluidized bed processing the most according to claim 1 and 2 is given up the equipment of Organic substance in water and heavy metal ion, and it is special Levy and be: the outside of described organic recovery room (2) is provided with the waterwater entrance (1) communicated therewith.
CN201620401144.2U 2016-05-06 2016-05-06 Useless organics in water and heavy metal ion's equipment is handled to microwave fluidized bed Expired - Fee Related CN205575858U (en)

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CN201620401144.2U CN205575858U (en) 2016-05-06 2016-05-06 Useless organics in water and heavy metal ion's equipment is handled to microwave fluidized bed

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Application Number Priority Date Filing Date Title
CN201620401144.2U CN205575858U (en) 2016-05-06 2016-05-06 Useless organics in water and heavy metal ion's equipment is handled to microwave fluidized bed

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106746104A (en) * 2016-11-14 2017-05-31 武汉兴天宇环境股份有限公司 A kind of household sewage processes recycle device
CN114105169A (en) * 2020-08-27 2022-03-01 上海市机电设计研究院有限公司 Purification treatment system and treatment method for solid waste salt

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106746104A (en) * 2016-11-14 2017-05-31 武汉兴天宇环境股份有限公司 A kind of household sewage processes recycle device
CN114105169A (en) * 2020-08-27 2022-03-01 上海市机电设计研究院有限公司 Purification treatment system and treatment method for solid waste salt

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C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20160914

Termination date: 20170506