CN106554113A - It is easy to the underground work liquid waste treatment system of non-pollution discharge - Google Patents

It is easy to the underground work liquid waste treatment system of non-pollution discharge Download PDF

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Publication number
CN106554113A
CN106554113A CN201610979811.XA CN201610979811A CN106554113A CN 106554113 A CN106554113 A CN 106554113A CN 201610979811 A CN201610979811 A CN 201610979811A CN 106554113 A CN106554113 A CN 106554113A
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ashes
reactor
treatment system
sent
waste treatment
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蒋遂安
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Chengdu Safety Environment Technology Co Ltd
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Chengdu Safety Environment Technology Co Ltd
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Priority to CN201610979811.XA priority Critical patent/CN106554113A/en
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/001Incinerators or other apparatus for consuming industrial waste, e.g. chemicals for sludges or waste products from water treatment installations
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/001Processes for the treatment of water whereby the filtration technique is of importance
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/40Devices for separating or removing fatty or oily substances or similar floating material
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/441Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/10Nature of the water, waste water, sewage or sludge to be treated from quarries or from mining activities

Abstract

The invention discloses it is easy to the underground work liquid waste treatment system of non-pollution discharge, including liquid waste treatment system and ejection processing system;The liquid waste treatment system includes reactor I and mixing storeroom;The reactor I carries out oxidation processes to mixed liquor, makes the macromolecule organic degraded in mixed liquor, so as to reduce mixing the material that links are produced in storeroom storage liquid waste treatment system described in the content of bichromate.The ejection processing system includes being sequentially communicated negative pressure of vacuum dewatering system combustion system and ashes processing system by transmission pipeline;The negative pressure of vacuum system carries out processed and will be dehydrated to mixed solution, and the combustion system carries out burning the discharge chamber by ashes feeding ashes processing system to powder, carries out the process of ashes.Ejection in underground work liquid waste treatment system is carried out follow-up pollution-freeization to process, the process problem of ejection is not only solved, it is thus also avoided that environmental pollution.

Description

It is easy to the underground work liquid waste treatment system of non-pollution discharge
Technical field
The present invention relates to a kind of liquid waste treatment system, and in particular to be easy to the underground work liquid waste processing system of non-pollution discharge System.
Background technology
Environmental conservation, referred to as environmental protection, refer to the mankind to solve reality or potential environmental problem, coordinate the mankind with environment Relation, the living environment for protecting the mankind, the sustainable development for ensureing economic society and the general name of various action taken.Environment is protected Shield mode includes:Administration, law, economy, science and technology, spontaneous environmental protection organization among the people etc. are taken, reasonably using money naturally Source, prevents the pollution and destruction of environment, in the hope of the same humanistic environment of natural environment, economic environment common equilibrium sustainable development, expands The reproduction of big useful resources, it is ensured that the development of society.In the underground work for excavating oil, can need using addition because of operation Agent, because causing substantial amounts of down-hole waste liquid.The complicated component of the fracturing wastewater of this down-hole, major pollutants be bichromate, Petroleum-type, ammonia nitrogen, float etc..If down-hole waste liquid is mixed into after mud pit filled on the spot, certainly will to on-site soil with Groundwater environment brings pollution hidden trouble.The liquid waste processing mode for adopting at present mainly has operation wastewater scene centralized processor, Will down-hole the recovered car of waste liquid collect after, reprocessing.The device can remove greasy dirt in the waste liquid of down-hole, float etc..But Adopt in this way, still containing materials influential on environment such as a certain amount of bichromates in the waste water after process, and The material for being unfavorable for direct discharge can be produced during disposing waste liquid.
The content of the invention
The technical problem to be solved is current liquid waste processing mode, still contains one in the waste water after process The material influential on environment such as quantitative bichromate, and can produce during disposing waste liquid and be unfavorable for directly discharge Material.Therefore it is an object of the invention to provide being easy to the underground work liquid waste treatment system of non-pollution discharge, solve current Liquid waste processing mode, still containing materials influential on environment such as a certain amount of bichromates in the waste water after process, and The problem of the material for being unfavorable for direct discharge can be produced during disposing waste liquid.
The present invention is achieved through the following technical solutions:
It is easy to the underground work liquid waste treatment system of non-pollution discharge, including underground work liquid waste treatment system, including by broken Steady agent device for supplying, flocculant device for supplying, oxidant device for supplying and the waste liquid being sequentially communicated by transport pipeline are stored Room, degreasing unit, broken steady room, flocculation plant, defecator, reactor I, reverse osmosis unit and mixing storeroom;It is described broken steady Agent device for supplying is connected with broken steady room, and supplies destabilizing agent to broken steady room;The flocculant device for supplying is connected with flocculation plant, And flocculant is supplied to flocculation plant;The oxidant device for supplying is connected with reactor I, and feeds oxidant to reactor I; Waste liquid from waste reservoirs is carried out oil removal treatment by the degreasing unit, and the greasy dirt obtained after process is sent into greasy dirt storage Room is hidden, oil-free waste liquid is sent into by water pump and breaks steady room;It is described to break steady room waste liquid is carried out broken surely to process, with destroying waste liquid and steady It is qualitative, it is easy to follow-up liquid waste processing, and the waste liquid after process is sent into into flocculation plant.Negatively charged cloudy grain in the waste liquid of down-hole Sub- polymer adsorbs in oil droplet and the surface of solids, and the stability of oil-water emulsion increases, and in making waste liquid, various composition is uniformly divided It is dispersed in waste liquid, is not easily disconnected from, and in the form of independence.Destabilizing agent is added to waste liquid, steady process is carried out brokenly, is then broken The stability of various composition in waste liquid, reduces the viscosity of dehydration body, is easy to follow-up liquid waste processing.The flocculation plant is by waste liquid In solid matter and solable matter carry out flocculation reaction, obtain the mixture being made up of flocculate and mixed liquor, and will wadding Solidifying reacted mixture sends into defecator.Flocculation sediment is the very economical feasible method in sewage, liquid waste processing, wadding Removal of the solidifying agent to float and petroleum-type is very effective.The defecator is filtered to mixture, by flocculate and mixed Close liquid to separate, and mixed liquor is sent into into reactor I;The reactor I carries out oxidation processes to mixed liquor, in making mixed liquor Macromolecule organic is degraded, and so as to reduce the content of bichromate, and the liquid after oxidation processes is sent into reverse osmosis unit.Oxygen Change process chamber by adding oxidant in mixed liquor so that the macromolecule organic degraded in waste liquid, so as to reduce dichromic acid A kind of method of salt.The liquid obtained after oxidation processes is carried out reverse-osmosis treated by the reverse osmosis unit, obtains concentrate solution With the penetrating fluid that can be discharged.Reverse osmosiss are the films point that a kind of skill by means of permselectivity membrane can be with pressure as motive force From technology, when pressure added in system is more than into aqueous solution osmotic pressure, hydrone constantly passes through film, through producing water flow passage Central canal is flowed into, then impurity at one end in outflow water, such as ion, Organic substance, antibacterial, virus etc., be trapped within entering for film Water side, then flows out in concentrated water water side, so as to reach isolation of purified purpose.The mixing storeroom and defecator, electrolysis Device connects, and the impurity that adsorbs on electrode in preserving the flocculate, electrolysis unit that defecator obtains and reverse osmosis unit The concentrate solution for obtaining.
The ejection processing system includes being sequentially communicated negative pressure of vacuum dewatering system, pulverizer, combustion by transmission pipeline Burning system, exsiccator, discharge chamber and ashes processing system;The negative pressure of vacuum dewatering system is connected with mixing storeroom, is mixed Mixed solution is sent to negative pressure of vacuum system by storeroom, and the negative pressure of vacuum system carries out processed and incites somebody to action to mixed solution The clod obtained after dehydration delivers to crushing system;Clod after dehydration is crushed by the crushing system, and after crushing The powder for arriving sends into combustion system;The combustion system is burnt to powder, and by the ashes obtained after burning and flue dust Send into exsiccator;Ashes and flue dust are dried by the exsiccator, and dried ashes and flue dust are sent into discharge chamber; Ashes are sent into ashes processing system by the discharge chamber, carry out the process of ashes.
Further, also including electrolysis unit, the electrolysis unit is arranged between reactor I and reverse osmosis unit, electricity Solution device is by the impurity absorption of suspended state and colloidal attitude in liquid on electrode.Electrolysis unit is by micro-electrolysis method by special body size Impurity absorption or be deposited on electrode, so as to remove the polluter of suspended state and colloidal attitude in liquid.
Further, the negative pressure of vacuum dewatering system includes reactor II, vacuum pump and condenser;The reactor II It is connected with mixing storeroom, vacuum pump, condenser and pulverizer respectively;Air in reactor II is taken away by vacuum pump, makes Reduced pressure in reactor II, so as to reduce the boiling point of mixed solution in reactor II, makes the water in mixed solution be changed into water Steam, discharges from condenser, and remaining solid matter in reactor II is sent into pulverizer;Condenser is played to water vital qi Cooling effect.At ambient pressure, the boiling point of general liquid is 100 degrees Celsius, but in the presence of vacuum pump, in reactor II Reduced pressure, the boiling point of the liquid in reactor II also follow decline, so that moisture is changed into vapor earlier and by cold Condenser is discharged.
Further, the ashes processing system includes storage ashpit, component detection apparatus and the brickmaking machine being sequentially communicated;Institute State storage ashpit to connect with discharge chamber, and the ashes of self-discharging in future room send into component detection apparatus;The component detection apparatus inspection The material that ashes whether there is contaminated soil is surveyed, if having, ashes is sent to brickmaking machine, conversely, ashes are directly discharged to mud then In soil.Brickmaking machine is the plant equipment for manufacturing and producing brick, typically using stone powder, flyash, slag, slag, rubble, sand, Water etc. adds machinery of the cement as raw material by the production brick such as hydraulic power, shaking force, aerodynamic force.In the invention, will Through dehydration, burning and the ashes being dried as the raw material for producing fragment of brick, one is the increase in underground work liquid waste treatment system Ejected matter use value, two is the raw material using ashes as fragment of brick, has saved cost of material.When there is no dirt in ashes During the pollutant of dye soil, directly by overall ash emission in soil, can use ashes as the soil of fertilizer or kind flower.
Further, also including air treatment system, the air treatment system includes the separator being sequentially communicated and sky Gas purifier, the separator are connected with discharge chamber and storage ashpit respectively, and dried flue dust is sent into separator by discharge chamber, point The gas in flue dust is separated with solid particle from device, and feeds gas into air purifier, solid particle is sent into into storage ashpit, The air purifier is arranged in air after purifying to the air in separator.Air purifier is to refer to inhale It is attached, decompose or convert various air pollutants, effectively improve the equipment of air cleanliness.
Further, the combustion system includes air pump and combustor;The combustor respectively with pulverizer, air The connection of pump, greasy dirt storeroom, exsiccator and screening machine;Air pump gives combustor auxiliary air, greasy dirt storeroom using greasy dirt as Combustion adjuvant is fed to combustor;Combustor is by the dust-firing from pulverizer, and the product after burning is sent into exsiccator.
Further, the exsiccator is rotary drier.Rotary drier is a kind of a large amount of materials of process Dry exsiccator.As operating is reliable, operating flexibility is big, strong adaptability, disposal ability are big, be widely used in metallurgy, building materials, The departments such as light industry.Rotary drier applies in general to granular material, it is also possible to which part mixes the method for dry material and is dried The higher material of viscosity plaster material or water content, and be successfully used in the granulating and drying of solution material.Powder is in burning In, can decompose and produce certain moisture, the ashes for having moisture are dried by exsiccator, are easy to the preparation of follow-up brick-making raw material.
Further, the separator is cyclone separator.Cyclone separator, is using solid in centrifugal force separate air-flow The equipment of granule or drop, is introduced tangentially into the rotary motion for causing by air-flow, makes the solid particle with larger centrifugal inertial force Or drop gets rid of to outside wall surface and separates.It is industrially to apply a kind of very wide separation equipment., in burning, a part can be with ash for powder In the form of cinder, another part then can be in the form of flue dust.Gas and solid granule in flue dust is divided by separator Leave, be not only convenient for follow-up purification of air, be also convenient for focusing on solid granule.
The present invention compared with prior art, has the following advantages and advantages:
1st, the present invention is easy to the underground work liquid waste treatment system of non-pollution discharge, by oxidation processes and reverse-osmosis treated, Impurity in waste liquid is discharged, to reach the standard that can be discharged, soil protection;
2nd, the present invention is easy to the underground work liquid waste treatment system of non-pollution discharge, the electrolysis dress arranged before reverse osmosis unit Put, further the impurity in liquid is excluded, more water for reaching discharge standard in being easy to reverse-osmosis treated, are can penetrate out;
3rd, the present invention is easy to the underground work liquid waste treatment system of non-pollution discharge, by the row in underground work liquid waste treatment system Going out thing carries out follow-up pollution-freeization process, not only solves the process problem of ejection, it is thus also avoided that environmental pollution.
Description of the drawings
Accompanying drawing described herein is used for providing further understanding the embodiment of the present invention, constitutes of the application Point, do not constitute the restriction to the embodiment of the present invention.In the accompanying drawings:
Fig. 1 is schematic structural view of the invention.
Specific embodiment
To make the object, technical solutions and advantages of the present invention become more apparent, with reference to embodiment and accompanying drawing, to this Invention is described in further detail, and the exemplary embodiment of the present invention and its explanation are only used for explaining the present invention, do not make For limitation of the invention.
Embodiment one
As shown in figure 1, the present invention is easy to the underground work liquid waste treatment system of non-pollution discharge, including underground work liquid waste processing System, including by destabilizing agent device for supplying, flocculant device for supplying, oxidant device for supplying and by transport pipeline successively The waste reservoirs of connection, degreasing unit, break steady room, flocculation plant, defecator, reactor I, reverse osmosis unit and mixing storage Hide room;The destabilizing agent device for supplying is connected with broken steady room, and supplies destabilizing agent to broken steady room;The flocculant device for supplying with Flocculation plant connects, and supplies flocculant to flocculation plant;The oxidant device for supplying is connected with reactor I, and to reaction Kettle I feeds oxidant;Waste liquid from waste reservoirs carries out oil removal treatment by the degreasing unit, and will obtain after process Greasy dirt sends into greasy dirt storeroom, and oil-free waste liquid is sent into by water pump and breaks steady room;The broken steady room carries out brokenly steady process to waste liquid, with Destruction waste liquid and stability, be easy to follow-up liquid waste processing, and the waste liquid after process sent into into flocculation plant.In the waste liquid of down-hole Negatively charged cloudy particulate polymer is adsorbed in oil droplet and the surface of solids, and the stability of oil-water emulsion increases, and makes each in waste liquid Plant composition to be uniformly dispersed in waste liquid, be not easily disconnected from, and in the form of independence.Destabilizing agent is added to waste liquid, is broken It is steady to process, then it is the stability for breaking various composition in waste liquid, reduces the viscosity of dehydration body, be easy to follow-up liquid waste processing.Institute Stating flocculation plant carries out flocculation reaction by the solid matter and solable matter in waste liquid, obtains being made up of flocculate and mixed liquor Mixture, and by after flocculation reaction mixture send into defecator.Flocculation sediment is the very Jing in sewage, liquid waste processing The feasible method of Ji, removal of the flocculant to float and petroleum-type are very effective.The defecator was carried out to mixture Filter, flocculate and mixed liquor are separated, and mixed liquor is sent into reactor I;The reactor I is carried out at oxidation to mixed liquor Reason, makes the macromolecule organic degraded in mixed liquor, so as to reduce the content of bichromate, and the liquid after oxidation processes is sent Enter reverse osmosis unit.Oxidation processes room is by adding oxidant in mixed liquor so that the macromolecule organic degraded in waste liquid, So as to reduce a kind of method of bichromate.During oxidation processes, hypochlorite is added in a liquid.Hypochlorite oxidation method is profit The oxidation processes of liquid are carried out with the strong oxidizing property of hypochlorite.While oxidation processes are carried out using hypochlorite, to liquid Body carries out ultra violet lamp, to accelerate oxidation reaction.The liquid obtained after oxidation processes is carried out reverse osmosis by the reverse osmosis unit Process thoroughly, obtain concentrate solution and the penetrating fluid that can be discharged.Reverse osmosiss are a kind of skill energy by means of permselectivity membrane Membrane separation technique with pressure as motive force, when pressure added in system is more than into aqueous solution osmotic pressure, hydrone is continuous Pass through film, flow into central canal through producing water flow passage, then impurity at one end in outflow water, such as ion, Organic substance, antibacterial, Virus etc., is trapped within the influent side of film, then flows out in concentrated water water side, so as to reach isolation of purified purpose.The mixing Storeroom is connected with defecator, electrolysis unit, and is adsorbed in electrode in preserving the flocculate, electrolysis unit that defecator obtains On the concentrate solution that obtains of impurity and reverse osmosis unit.
The ejection processing system includes being sequentially communicated negative pressure of vacuum dewatering system, pulverizer, combustion by transmission pipeline Burning system, exsiccator, discharge chamber and ashes processing system;The negative pressure of vacuum dewatering system is connected with mixing storeroom, is mixed Mixed solution is sent to negative pressure of vacuum system by storeroom, and the negative pressure of vacuum system carries out processed and incites somebody to action to mixed solution The clod obtained after dehydration delivers to crushing system;Clod after dehydration is crushed by the crushing system, and after crushing The powder for arriving sends into combustion system;The combustion system is burnt to powder, and by the ashes obtained after burning and flue dust Send into exsiccator;Ashes and flue dust are dried by the exsiccator, and dried ashes and flue dust are sent into discharge chamber; Ashes are sent into ashes processing system by the discharge chamber, carry out the process of ashes.
Further, also including electrolysis unit, the electrolysis unit is arranged between reactor I and reverse osmosis unit, electricity Solution device is by the impurity absorption of suspended state and colloidal attitude in liquid on electrode.Electrolysis unit is by micro-electrolysis method by special body size Impurity absorption or be deposited on electrode, so as to remove the polluter of suspended state and colloidal attitude in liquid.
Further, the negative pressure of vacuum dewatering system includes reactor II, vacuum pump and condenser;The reactor II It is connected with mixing storeroom, vacuum pump, condenser and pulverizer respectively;Air in reactor II is taken away by vacuum pump, makes Reduced pressure in reactor II, so as to reduce the boiling point of mixed solution in reactor II, makes the water in mixed solution be changed into water Steam, discharges from condenser, and remaining solid matter in reactor II is sent into pulverizer;Condenser is played to water vital qi Cooling effect.At ambient pressure, the boiling point of general liquid is 100 degrees Celsius, but in the presence of vacuum pump, in reactor II Reduced pressure, the boiling point of the liquid in reactor II also follow decline, so that moisture is changed into vapor earlier and by cold Condenser is discharged.At one atm, the boiling temperature of water is 100 degrees Celsius.When pressure is less than an atmospheric pressure, the boiling of water Point is lower than 100 degrees Celsius:When pressure is 0.7 atmospheric pressure, the boiling point of water is 90 degrees Celsius;Pressure is 0.3 atmospheric pressure When, the boiling point of water is 70 degrees Celsius;When pressure is 0.1 atmospheric pressure, the boiling point of water is 40 degrees Celsius.
Further, the ashes processing system includes storage ashpit, component detection apparatus and the brickmaking machine being sequentially communicated;Institute State storage ashpit to connect with discharge chamber, and the ashes of self-discharging in future room send into component detection apparatus;The component detection apparatus inspection The material that ashes whether there is contaminated soil is surveyed, if having, ashes is sent to brickmaking machine, conversely, ashes are directly discharged to mud then In soil.Brickmaking machine is the plant equipment for manufacturing and producing brick, typically using stone powder, flyash, slag, slag, rubble, sand, Water etc. adds machinery of the cement as raw material by the production brick such as hydraulic power, shaking force, aerodynamic force.In the invention, will Through dehydration, burning and the ashes being dried as the raw material for producing fragment of brick, one is the increase in underground work liquid waste treatment system Ejected matter use value, two is the raw material using ashes as fragment of brick, has saved cost of material.When there is no dirt in ashes During the pollutant of dye soil, directly by overall ash emission in soil, can use ashes as the soil of fertilizer or kind flower.
Further, also including air treatment system, the air treatment system includes the separator being sequentially communicated and sky Gas purifier, the separator are connected with discharge chamber and storage ashpit respectively, and dried flue dust is sent into separator by discharge chamber, point The gas in flue dust is separated with solid particle from device, and feeds gas into air purifier, solid particle is sent into into storage ashpit, The air purifier is arranged in air after purifying to the air in separator.Air purifier is to refer to inhale It is attached, decompose or convert various air pollutants, effectively improve the equipment of air cleanliness.
Further, the combustion system includes air pump and combustor;The combustor respectively with pulverizer, air The connection of pump, greasy dirt storeroom, exsiccator and screening machine;Air pump gives combustor auxiliary air, greasy dirt storeroom using greasy dirt as Combustion adjuvant is fed to combustor;Combustor is by the dust-firing from pulverizer, and the product after burning is sent into exsiccator.
Further, the exsiccator is rotary drier.Rotary drier is a kind of a large amount of materials of process Dry exsiccator.As operating is reliable, operating flexibility is big, strong adaptability, disposal ability are big, be widely used in metallurgy, building materials, The departments such as light industry.Rotary drier applies in general to granular material, it is also possible to which part mixes the method for dry material and is dried The higher material of viscosity plaster material or water content, and be successfully used in the granulating and drying of solution material.Powder is in burning In, can decompose and produce certain moisture, the ashes for having moisture are dried by exsiccator, are easy to the preparation of follow-up brick-making raw material.
Further, the separator is cyclone separator.Cyclone separator, is using solid in centrifugal force separate air-flow The equipment of granule or drop, is introduced tangentially into the rotary motion for causing by air-flow, makes the solid particle with larger centrifugal inertial force Or drop gets rid of to outside wall surface and separates.It is industrially to apply a kind of very wide separation equipment., in burning, a part can be with ash for powder In the form of cinder, another part then can be in the form of flue dust.Gas and solid granule in flue dust is divided by separator Leave, be not only convenient for follow-up purification of air, be also convenient for focusing on solid granule.
Embodiment two
The present embodiment is illustrating to the experiment done on the basis of embodiment one.
Realize object:2000L repaiies well-flushing waste liquid, and its process step is as follows:
1st, waste liquid feeding oil discharging device is carried out into oil removal treatment, greasy dirt is sent into into greasy dirt storeroom, the waste liquid after oil removing is sent into broken Degreasing 150L is removed in steady room, the step;
2nd, break steady room carries out broken steady process to waste liquid, with destroying waste liquid and stability, and will it is broken it is steady after waste liquid send into and flocculate Device;
3rd, flocculation plant carries out liquid waste processing to waste liquid, adds 13kgPAC and 11kgPAJ as flocculant, and stir toward waste liquid After mixing reaction 20min, flocculate and liquid are obtained;To liquid measure, in waste liquid, bichromate reduces 73%, then by waste liquid Send into defecator;
4th, defecator is filtered to waste liquid, and flocculate is sent into mixing storeroom, and liquid sends into reactor;
5th, the hypochlorite of 90mg is added in a kettle., is irradiated and after stirring reaction 30min, to which in being placed in Burdick lamp Measure, the bichromate in waste liquid reduces 81.3% on the basis of before, and liquid is sent into electrolysis unit then;
6th, electrolysis unit adopt Fe/C micro-electrolysis methods, Fe/C volume ratios be 1.5, ferrum Resina Draconis degree be 60-80 mesh, ammonium chloride dosage For 1850mg, Jing after with Fe/C light electrolysis, liquid chroma removal rate 95%, bichromate is reduced on the basis of previous step 58%, liquid is sent into into reverse osmosis unit then, the impurity adsorbed on electrolysis unit electrode sends into mixing storeroom;
7th, the water in liquid can be appeared, water with pressure as motive force by reverse osmosis unit by means of the skill of permselectivity membrane In impurity, such as ion, Organic substance etc. are trapped within the influent side of film, then directly discharge the water for appearing, containing impurity Water sends into mixing storeroom.Finally, process complete can qualified discharge water be 1.8L, the material accounting not directly discharged is very It is little.
The 8th, the 500L mixture of repeatedly accumulation storage is sent into the reaction in negative pressure of vacuum dewatering system from mixing storeroom Kettle, vacuum pump are evacuated to reactor, and the atmospheric pressure in reactor is changed into 0.5 atmospheric pressure, and then reactor is in which Mixture heating, when being heated to 50 DEG C, the moisture in mixture be changed into vapor from condenser flow out;Mixture is deviate from After processing 20min, moisture is had been processed substantially, and mixture forms caking because of dehydration, and caking is sent into pulverizer, caking then Gross weight be 300kg;
9th, the caking sent is ground into powder by pulverizer, and sends into combustor;
10th, the greasy dirt processed out in underground work liquid waste treatment system is sent into into combustor from greasy dirt storeroom, as combustion adjuvant Use, while air pump provides sufficient air for combustor, be easy to what is burnt to be smoothed out;Ashes and cigarette are formed after dust-firing Dirt, and certain moisture is carried, ashes and flue dust are sent into into rotary drier;
11st, rotary drier is dried to the product after clod burning, is sent to discharge chamber after the completion of being dried;
12nd, discharge chamber carries out discharging to the material sent, and ashes are sent into storage ashpit, and flue dust sends into the rotation in air treatment system Wind separator;
13rd, the solid particle and gas in flue dust is separated by cyclone separator by centrifugal force, solid particle is sent into and is store Ashpit, feeds gas into air purifier;According to measurement, show that the 500L mixture is produced Jing after processing, burn in flue dust Solid particle weight be 0.5kg, by cyclone separator, not only the solid in flue dust can be collected, be easy to follow-up Process, also add the service life of air purifier, without be replaced as frequently as or scavenging air depurator the correlation such as filter element Device;
14th, air purifier is purified to the gas sent, and adsorbs the material for being not easy to direct discharge in gas, then Gas is discharged in air;
15th, the mixture for storing the solid particle of the ashes and cyclone separator of ashpit self-discharging in future room is sent into into composition detection dress Put, the material for being not easy to discharge of environment in component detection apparatus detection mixture, whether is polluted containing heavy metal etc.;After testing, There are the heavy metals such as chromium, copper in mixture, it is impossible to directly discharge, therefore mixture is sent into into brickmaking machine.Jing is measured, 500L mixture Ultimately form the ashes of 300kg.Although the material containing heavy metal is although harmful, and it is then to make use of weight by its brickmaking Standard of the dissolution of metal less than Environmental Protection Administration, therefore the products such as harmless haydite, water-permeable brick can be manufactured.
Above-described specific embodiment, has been carried out further to the purpose of the present invention, technical scheme and beneficial effect Describe in detail, the be should be understood that specific embodiment that the foregoing is only the present invention is not intended to limit the present invention Protection domain, all any modification, equivalent substitution and improvements within the spirit and principles in the present invention, done etc. all should include Within protection scope of the present invention.

Claims (8)

1. the underground work liquid waste treatment system of non-pollution discharge is easy to, it is characterised in that:Including liquid waste treatment system and discharge Thing processing system;
Wherein, the liquid waste treatment system is included by destabilizing agent device for supplying, flocculant device for supplying, oxidant device for supplying And be sequentially communicated by transport pipeline waste reservoirs, degreasing unit, broken steady room, flocculation plant, defecator, reactor Ith, reverse osmosis unit and mixing storeroom;The destabilizing agent device for supplying is connected with broken steady room, and supplies destabilizing agent to broken steady room; The flocculant device for supplying is connected with flocculation plant, and supplies flocculant to flocculation plant;The oxidant device for supplying with Reactor I connects, and feeds oxidant to reactor I;Waste liquid from waste reservoirs is carried out oil removing by the degreasing unit Process, and the greasy dirt obtained after process is sent into into greasy dirt storeroom, oil-free waste liquid is sent into by water pump and breaks steady room;It is described to break steady room Steady process is carried out brokenly to waste liquid, with destroying waste liquid and stability, is easy to follow-up liquid waste processing, and the waste liquid after process is sent Enter flocculation plant;Solid matter and solable matter in waste liquid is carried out flocculation reaction by the flocculation plant, is obtained by flocculating The mixture of thing and mixed liquor composition, and the mixture after flocculation reaction is sent into into defecator;The defecator is to mixing Thing is filtered, and flocculate and mixed liquor are separated, and mixed liquor is sent into reactor I;The reactor I enters to mixed liquor Row oxidation processes, make the macromolecule organic degraded in mixed liquor, so as to reduce the content of bichromate, and by after oxidation processes Liquid send into reverse osmosis unit;The liquid obtained after oxidation processes is carried out reverse-osmosis treated by the reverse osmosis unit, is obtained Concentrate solution and the penetrating fluid that can be discharged;The mixing storeroom is connected with defecator, electrolysis unit, and preserves filtration dress Put the flocculate for obtaining, the concentrate solution that the impurity and reverse osmosis unit adsorbed on electrode in electrolysis unit is obtained;
The ejection processing system includes being sequentially communicated negative pressure of vacuum dewatering system, pulverizer, burning system by transmission pipeline System, exsiccator, discharge chamber and ashes processing system;The negative pressure of vacuum dewatering system is connected with mixing storeroom, mixing storage Mixed solution is sent to negative pressure of vacuum system by room, and the negative pressure of vacuum system carries out processed and will be dehydrated to mixed solution The clod for obtaining afterwards delivers to crushing system;Clod after dehydration is crushed by the crushing system, and will be obtained after crushing Powder sends into combustion system;The combustion system is burnt to powder, and the ashes obtained after burning and flue dust are sent into Exsiccator;Ashes and flue dust are dried by the exsiccator, and dried ashes and flue dust are sent into discharge chamber;It is described Ashes are sent into ashes processing system by discharge chamber, carry out the process of ashes.
2. the underground work liquid waste treatment system for being easy to non-pollution discharge according to claim 1, it is characterised in that:Also wrap Electrolysis unit is included, the electrolysis unit is arranged between reactor I and reverse osmosis unit, electrolysis unit is by the suspended state in liquid With the impurity absorption of colloidal attitude on electrode.
3. the underground work liquid waste treatment system for being easy to non-pollution discharge according to claim 1, it is characterised in that:It is described Negative pressure of vacuum dewatering system includes reactor II, vacuum pump and condenser;The reactor II with mix storeroom, vacuum pump, Condenser and pulverizer connect respectively;Air in reactor II is taken away by vacuum pump, makes the reduced pressure in reactor II, So as to reduce the boiling point of mixed solution in reactor II, make the water in mixed solution be changed into vapor, discharge from condenser, and Remaining solid matter in reactor II is sent into into pulverizer;Condenser plays cooling effect to water vital qi.
4. the underground work liquid waste treatment system for being easy to non-pollution discharge according to claim 1, it is characterised in that:It is described Ashes processing system includes storage ashpit, component detection apparatus and the brickmaking machine being sequentially communicated;The storage ashpit is connected with discharge chamber, And the ashes of self-discharging in future room send into component detection apparatus;The component detection apparatus detection ashes have contamination-free, if having Pollutant, then send ashes to brickmaking machine, conversely, then ashes are directly discharged in soil.
5. the underground work liquid waste treatment system for being easy to non-pollution discharge according to claim 4, it is characterised in that:Also wrap Air treatment system is included, the air treatment system includes the separator being sequentially communicated and air purifier, the separator point Not with discharge chamber and storage ashpit connect, discharge chamber by dried flue dust send into separator, separator by the gas in flue dust with Solid particle is separated, and feeds gas into air purifier, and solid particle sent into storage ashpit, the air purifier to from Air in separator is arranged in air after being purified.
6. the underground work liquid waste treatment system for being easy to non-pollution discharge according to claim 1, it is characterised in that:It is described Combustion system includes air pump and combustor;The combustor is connected with pulverizer, air pump, greasy dirt storeroom and exsiccator respectively Connect;Air pump is fed to combustor using greasy dirt as combustion adjuvant to combustor auxiliary air, greasy dirt storeroom;Combustor will be from The dust-firing of pulverizer, and the product after burning is sent into into exsiccator.
7. the underground work liquid waste treatment system for being easy to non-pollution discharge according to claim 1, it is characterised in that:It is described Exsiccator is rotary drier.
8. the underground work liquid waste treatment system for being easy to non-pollution discharge according to claim 5, it is characterised in that:It is described Separator is cyclone separator.
CN201610979811.XA 2016-11-08 2016-11-08 It is easy to the underground work liquid waste treatment system of non-pollution discharge Pending CN106554113A (en)

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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101475285A (en) * 2009-01-19 2009-07-08 辽宁天意实业股份有限公司 Gas field sewerage and solid pollutant comprehensive processing technological process
CN101690937A (en) * 2008-04-30 2010-04-07 濮阳市天地人环保工程技术有限公司 Process technology for treating drilling waste while drilling before falling onto ground in oil-gas fields
CN102322642A (en) * 2011-06-07 2012-01-18 创冠环保(中国)有限公司 Sludge drying and incinerating system on basis of incineration of waste grate furnace and treatment method thereof

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101690937A (en) * 2008-04-30 2010-04-07 濮阳市天地人环保工程技术有限公司 Process technology for treating drilling waste while drilling before falling onto ground in oil-gas fields
CN101475285A (en) * 2009-01-19 2009-07-08 辽宁天意实业股份有限公司 Gas field sewerage and solid pollutant comprehensive processing technological process
CN102322642A (en) * 2011-06-07 2012-01-18 创冠环保(中国)有限公司 Sludge drying and incinerating system on basis of incineration of waste grate furnace and treatment method thereof

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Application publication date: 20170405