CN205347067U - Chemistry pail pack washing wastewater's modularization processing system - Google Patents
Chemistry pail pack washing wastewater's modularization processing system Download PDFInfo
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- CN205347067U CN205347067U CN201620020781.5U CN201620020781U CN205347067U CN 205347067 U CN205347067 U CN 205347067U CN 201620020781 U CN201620020781 U CN 201620020781U CN 205347067 U CN205347067 U CN 205347067U
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Abstract
The utility model belongs to chemistry pail pack washing wastewater's modularization processing system in the waste water treatment field comprises biochemical processing module of waste water collection module, waste water materialization processing module, waste water and waste water degree of depth processing module, and waste water collection module and waste water materialization processing module are connected, and waste water materialization processing module and waste water biochemistry processing module are connected, and waste water biochemistry processing module be connected with waste water degree of depth processing module, and waste water biochemistry processing module comprise good oxygen pond and anaerobism pond, the advanced waste treatment module is connected with the discharge port. The utility model provides a chemistry pail pack washing wastewater's modularization processing system adaptability is wide, the simple and convenient flexibility of operation management, and the low cost, the treatment effect is stabilized up to standardly.
Description
Technical field
This utility model belongs to field of waste water treatment, is specifically related to a kind of chemical packs barrelling and cleans the modularized treatment system of waste water.
Background technology
Chemical packs barrelling refers to all kinds of barreled packing container, storing solid, liquid and semi liquid state thickness chemicals, relates to organic, Inorganic Chemicals, product, and wherein organic quantity is big, of a great variety.A large amount of pail packs are many by the spontaneous collection of enterprise for a long time, clean and sell, and the waste water containing various chemicals is arbitrarily discharged, and thereby results in contamination accident and often occurs, and polluted-water threatens the safety of ecological environment.Technique is processed in particular without being specifically designed for the maturation cleaning waste water, only a certain or several industrial chemicals produces the process of waste water and reports to some extent, such as ferrum carbon electrolysis, anaerobic process, activated sludge process, contact oxidation method and SBR(sequencing batch active sludge) technique and these technical foundation are improved and the technique of coupling, its feature is be equipped with materialization means oxidation effect on the basis that anaerobic-aerobic is biochemical, although the feature of being respectively arranged with, but there is also following shortcoming: 1. energy consumption is high, operating cost is high；2. operation management is complicated；3. sludge output is big, it is possible to cause secondary pollution problem；4. the Industrial Wastewater Treatment weak effect of biochemical degradation it is difficult to；5. it is difficult to reach the standard of Treated sewage reusing.
Summary of the invention
The purpose of this utility model is in that to overcome the maturation not being specifically designed for cleaning waste water in prior art to process technique, common process process operation is costly, operation management is complicated, the defect that treatment effeciency is relatively low, a kind of wide adaptability is provided, operation management is easy flexibly, low cost, and the modularized treatment system of waste water is cleaned in the chemical packs barrelling for the treatment of effect stably reaching standard.
The purpose of this utility model is achieved through the following technical solutions:
The modularized treatment system of waste water is cleaned in chemical packs barrelling of the present utility model, it is made up of sewage collection module, waste water physicochemical processing module, wastewater biochemical processing module and Sewage advanced treatment module, it is characterized in that sewage collection module is connected with waste water physicochemical processing module, and be connected with wastewater biochemical processing module and Sewage advanced treatment module respectively by surmounting pipe；Sewage collection module is made up of wastewater collection pond group, and each wastewater collection pond in the group of wastewater collection pond is connected in parallel；Waste water physicochemical processing module is connected with wastewater biochemical processing module, and is connected with Sewage advanced treatment module or floss hole by surmounting pipe；Waste water physicochemical processing module is made up of materializing strategy submodule group, and each submodule in materializing strategy submodule group is connected in parallel, and module internal reflux pipe is connected with module inlet and module outlet respectively；Wastewater biochemical processing module is connected with Sewage advanced treatment module or is connected with floss hole by surmounting pipe；Wastewater biochemical processing module is made up of Aerobic Pond and anaerobic pond；Sewage advanced treatment module is connected with floss hole；Sewage advanced treatment module is made up of advanced treating submodule group, and each submodule in advanced treating submodule group is connected in parallel, and module internal reflux pipe is connected with module inlet and module outlet respectively.
In such scheme, described wastewater collection pond group is made up of acid waste water collecting pit, alkaline waste water collecting pit, oils wastewater collection pond, esters wastewater collection pond, benzene class wastewater collection pond, halohydrocarbon wastewater collection pond, heavy metal wastewater thereby collecting pit, amine wastewater collection pond and standby pool.
In such scheme, described materializing strategy submodule group by pH regulator submodule, coagulating sedimentation submodule, air supporting submodule, filter submodule, stripping submodule, sonochemical oxidation submodule, wet oxidation submodule, electrochemical oxidation submodule and Fenton(Fenton) aoxidize submodule and form.
In such scheme, described advanced treating submodule group is processed submodule, activated carbon adsorption submodule, electrochemical oxidation submodule, underload biochemical treatment submodule, ozone oxidation submodule and filtration submodule formed by resin absorption submodule, ion recon module, film.
In such scheme, pH regulator submodule in described materializing strategy submodule group is sequentially connected with is formed by mixed collection pond, pH regulator pond and intermediate pool, coagulating sedimentation submodule is sequentially connected with is formed by mixed collection pond, coagulating sedimentation facility and intermediate pool, air supporting submodule is sequentially connected with is formed by mixed collection pond, air supporting facility and intermediate pool, filtration submodule is sequentially connected with by mixed collection pond, filtration facility and intermediate pool and forms, and stripping submodule is sequentially connected with is formed by mixed collection pond, stripping facility and intermediate pool；Sonochemical oxidation submodule is sequentially connected with is formed by mixed collection pond, sonochemical oxidation facility and intermediate pool；Wet oxidation submodule is sequentially connected with is formed by mixed collection pond, wet oxidation facility and intermediate pool；Electrochemical oxidation submodule is sequentially connected with is formed by mixed collection pond, electrochemical oxidation facility and intermediate pool；Fenton oxidation submodule is sequentially connected with is formed by mixed collection pond, Fenton oxidation facility and intermediate pool.
In such scheme, the resin absorption submodule in described advanced treating submodule group is connected to form by mixed collection pond and resin absorption facility；Ion recon module is connected to form by mixed collection pond and ion commutating device；Film processes submodule and is connected to form by mixed collection pond and film treatment facility；Activated carbon adsorption submodule is connected to form by mixed collection pond and activated carbon adsorption facility；Electrochemical oxidation submodule is connected to form by mixed collection pond and electrochemical oxidation facility；Underload biochemical treatment submodule is connected to form by mixed collection pond and underload biochemical treatment facility；Ozone oxidation submodule is connected to form by mixed collection pond and ozone oxidation facility；Filter submodule to be connected to form by mixed collection pond and filtration facility.
The structures that to be in sewage disposal factory conventional such as pH regulator pond in materializing strategy submodule group, coagulative precipitation tank, air supporting facility, stripping facility, chemical oxidation, wet oxidation, the above-mentioned facility that this utility model is mentioned there is no particularity.
The cell body that pH regulator pond, coagulative precipitation tank and brick pond, concrete sump or other material are constructed, is equipped with dosing facility.
Air supporting facility is generally integration apparatus, is that a class passes in water or produces substantial amounts of micro air bubble, thus realizing the conventional water treatment facilities of solid-liquid separation.
Filtration facility is remove a kind of facility of float in waste water, fills screen cloth, sand, filter cloth, microporous pipe etc., be trapped more than the float of pore-size, make waste water obtain a degree of purification in cell body.
Stripping facility is conventional for stripping tower, is used for removing in water dissolved gas and volatile material, is passed into by gas in water, so as to be fully contacted mutually, making gas dissolved water and volatile material through gas-liquid interface, shifting to gas phase, thus removing pollutant.
Chemical oxidation, wet oxidation, electrochemical oxidation, Fenton oxidation facility are that high-level oxidation technology is also known as doing advanced oxidation processes, to produce the hydroxyl radical free radical (OH) with Strong oxdiative ability for feature, under the reaction conditions such as High Temperature High Pressure, electricity, sound, photoirradiation, catalyst, macromole hardly degraded organic substance is made to be oxidized to low toxicity or nontoxic small-molecule substance.
The structures that to be in sewage disposal factory conventional such as resin absorption facility in advanced treating submodule group, ion commutating device, film treatment facility, electrochemical oxidation facility, the above-mentioned facility that this utility model is mentioned there is no particularity.
Resin absorption facility is generally adsorption column, namely fills the resin sorbent with porous three dimensional structure in cylinder.
Ion commutating device swaps with the ion in weak solution by means of the ion in Solid-state Ion-exchange agent, and to reach to extract or remove the purpose of some ion in solution, main Types has agitator tank, fixed-bed ion exchanger, moving-bed ion exchange device etc..
Film treatment facility is the separation of the different component utilizing the Selective Separation of film to realize feed liquid, purification, concentration, and what frequently involve in advanced treating is microfiltration, ultrafiltration, nanofiltration, and reverse osmosis.
Activated carbon adsorption facility, namely fills activated carbon in structures, utilizes the absorption property of activated carbon, remove the polluter in sewage.
Underload biochemical treatment facility refers to the biochemical treatment facility of dwell period growth, underrun.
Ozone oxidation facility is to make oxidant with ozone waste water is purified and disinfects.
Work process of the present utility model is as follows:
According to the classification of chemical substance in pail pack, entering different cleaning sections, the waste water of generation enters in the corresponding collecting pit in sewage collection module, as wastewater property is identical, maybe can adopt materializing strategy technique of the same race, then can enter same collecting pit.
Waste water is subsequently into waste water physicochemical processing module, after a certain materializing strategy technique (neutralization, precipitation, air supporting, stripping, advanced oxidation etc.), as processed not up to given requirements, then re-enter into another materializing strategy technique by module internal reflux system, and can continuous circular treatment, until it reaches expection treatment effect；When waste water is made without materializing strategy, waste water physicochemical processing module can be surmounted, enter wastewater biochemical processing module either directly through surmounting pipe.
Waste water quality is different, the group technology kind adopted is different, but the processing sequence of wastewater treatment should proceed as follows: pH regulator facility, stripping facility, air supporting facility, oxidation facility (Fenton oxidation, wet oxidation, sonochemical oxidation, electrochemical oxidation), coagulating sedimentation facility etc..
After waste water entrance wastewater biochemical processing module after " anaerobism+aerobic " processes, if effluent quality meets requirement, then can directly discharging, what be unsatisfactory for requirement then can enter corresponding Sewage advanced treatment module process section.
Sewage advanced treatment module is provided with multiple techniques such as absorption, ion exchange, film process, identical with waste water physicochemical processing module, by arranging return duct, it is possible to what realize waste water repeats process, so that water quality reaching standard.
The beneficial effects of the utility model are in that:
Owing to waste water is cleaned in chemical packs barrelling, to relate to chemical class numerous and diverse, and water quality is changeable, and is all difficult to process, adopt single technique that wastewater to reach standard often cannot be made to process, it is proposed that the modularized processing concept of waste water, namely each processing unit is synergic system, but not a set of technique is exclusive, can independent assortment between each processing unit, many set waste water combined treatment process can occur, compare traditional handicraft, it is possible to decrease structures build cost, saving expense, also can reach good treatment effect.Also New raxa waste water can be carried out test pretreatment, to determine appropriate process simultaneously.Whole Waste Water Treatment is divided into sewage collection module, waste water physicochemical processing module, wastewater biochemical processing module, Sewage advanced treatment module, all includes the submodule of different process combination, also can carry out respective combination between each submodule in each module.Character according to waste water, by PLC(programmable logic controller (PLC)) control system, by the control that each pipeline valve is switched, it is achieved the combination of different process, embody the motility of technique.Arranging detection system in each module water side, waste water quality is detected, when meeting lower process section inflow requirement, just can enter next process section and process, otherwise the return-flow system by arranging in module proceeds to process.A kind of waste water correspondence one processes program, by the switch of PLC autocontrol valve, it is achieved the automatization of wastewater treatment.So, take combined type, the process system of switchable Alternative section is core of the present utility model.
Therefore, this utility model overcomes and is not specifically designed for the maturation process technique cleaning waste water in prior art, common process process operation is costly, operation management is complicated, the defect that treatment effeciency is relatively low, it is provided that chemical packs barrelling clean the modularized treatment system wide adaptability of waste water, operation management is easy flexibly, low cost, treatment effect stably reaching standard.
Accompanying drawing explanation
Fig. 1 is schematic diagram of the present utility model.
Fig. 2 is submodule schematic diagram of the present utility model.
Detailed description of the invention
It is described in further detail this utility model below in conjunction with drawings and Examples, but this utility model is not limited only to described embodiment.
Embodiment one
The modularized treatment system of the chemical packs barrelling cleaning waste water of this example is as depicted in figs. 1 and 2, it is made up of sewage collection module, waste water physicochemical processing module, wastewater biochemical processing module and Sewage advanced treatment module, it is characterized in that sewage collection module is connected with waste water physicochemical processing module, and be connected with wastewater biochemical processing module and Sewage advanced treatment module respectively by surmounting pipe；Sewage collection module is made up of wastewater collection pond group, and each wastewater collection pond in the group of wastewater collection pond is connected in parallel；Waste water physicochemical processing module is connected with wastewater biochemical processing module, and is connected with Sewage advanced treatment module or floss hole by surmounting pipe；Waste water physicochemical processing module is made up of materializing strategy submodule group, and each submodule in materializing strategy submodule group is connected in parallel, and module internal reflux pipe is connected with module inlet and module outlet respectively；Wastewater biochemical processing module is connected with Sewage advanced treatment module or is connected with floss hole by surmounting pipe；Wastewater biochemical processing module is made up of two-stage anaerobic pond；Sewage advanced treatment module is connected with floss hole；Sewage advanced treatment module is made up of advanced treating submodule group, and each submodule in advanced treating submodule group is connected in parallel, and module internal reflux pipe is connected with module inlet and module outlet respectively.
Wherein, wastewater collection pond group is made up of acid waste water collecting pit, alkaline waste water collecting pit, oils wastewater collection pond, esters wastewater collection pond, benzene class wastewater collection pond, halohydrocarbon wastewater collection pond, heavy metal wastewater thereby collecting pit, amine wastewater collection pond and standby pool.
Materializing strategy submodule group by pH regulator submodule, coagulating sedimentation submodule, air supporting submodule, filter submodule, stripping submodule, sonochemical oxidation submodule, wet oxidation submodule, electrochemical oxidation submodule and Fenton(Fenton) aoxidize submodule and form.
Advanced treating submodule group is processed submodule, activated carbon adsorption submodule, electrochemical oxidation submodule, underload biochemical treatment submodule, ozone oxidation submodule and filtration submodule formed by resin absorption submodule, ion recon module, film.
PH regulator submodule in materializing strategy submodule group is sequentially connected with is formed by mixed collection pond, pH regulator pond and intermediate pool, coagulating sedimentation submodule is sequentially connected with is formed by mixed collection pond, coagulating sedimentation facility and intermediate pool, air supporting submodule is sequentially connected with is formed by mixed collection pond, air supporting facility and intermediate pool, filtration submodule is sequentially connected with by mixed collection pond, filtration facility and intermediate pool and forms, and stripping submodule is sequentially connected with is formed by mixed collection pond, stripping facility and intermediate pool；Sonochemical oxidation submodule is sequentially connected with is formed by mixed collection pond, sonochemical oxidation facility and intermediate pool；Wet oxidation submodule is sequentially connected with is formed by mixed collection pond, wet oxidation facility and intermediate pool；Electrochemical oxidation submodule is sequentially connected with is formed by mixed collection pond, electrochemical oxidation facility and intermediate pool；Fenton oxidation submodule is sequentially connected with is formed by mixed collection pond, Fenton oxidation facility and intermediate pool.
Resin absorption submodule in advanced treating submodule group is connected to form by mixed collection pond and resin absorption facility；Ion recon module is connected to form by mixed collection pond and ion commutating device；Film processes submodule and is connected to form by mixed collection pond and film treatment facility；Activated carbon adsorption submodule is connected to form by mixed collection pond and activated carbon adsorption facility；Electrochemical oxidation submodule is connected to form by mixed collection pond and electrochemical oxidation facility；Underload biochemical treatment submodule is connected to form by mixed collection pond and underload biochemical treatment facility；Ozone oxidation submodule is connected to form by mixed collection pond and ozone oxidation facility；Filter submodule to be connected to form by mixed collection pond and filtration facility.
The structures that to be in sewage disposal factory conventional such as pH regulator pond in materializing strategy submodule group, coagulative precipitation tank, air supporting facility, stripping facility, chemical oxidation, wet oxidation, the above-mentioned facility that the present invention mentions there is no particularity.
The cell body that pH regulator pond, coagulative precipitation tank and brick pond, concrete sump or other material are constructed, is equipped with dosing facility.
Air supporting facility is generally integration apparatus, is that a class passes in water or produces substantial amounts of micro air bubble, thus realizing the conventional water treatment facilities of solid-liquid separation.
Filtration facility is remove a kind of facility of float in waste water, fills screen cloth, sand, filter cloth, microporous pipe etc., be trapped more than the float of pore-size, make waste water obtain a degree of purification in cell body.
Stripping facility is conventional for stripping tower, is used for removing in water dissolved gas and volatile material, is passed into by gas in water, so as to be fully contacted mutually, making gas dissolved water and volatile material through gas-liquid interface, shifting to gas phase, thus removing pollutant.
Chemical oxidation, wet oxidation, electrochemical oxidation, Fenton oxidation facility are that high-level oxidation technology is also known as doing advanced oxidation processes, to produce the hydroxyl radical free radical (OH) with Strong oxdiative ability for feature, under the reaction conditions such as High Temperature High Pressure, electricity, sound, photoirradiation, catalyst, macromole hardly degraded organic substance is made to be oxidized to low toxicity or nontoxic small-molecule substance.
The structures that to be in sewage disposal factory conventional such as resin absorption facility in advanced treating submodule group, ion commutating device, film treatment facility, electrochemical oxidation facility, the above-mentioned facility that the present invention mentions there is no particularity.
Resin absorption facility is generally adsorption column, namely fills the resin sorbent with porous three dimensional structure in cylinder.
Ion commutating device swaps with the ion in weak solution by means of the ion in Solid-state Ion-exchange agent, and to reach to extract or remove the purpose of some ion in solution, main Types has agitator tank, fixed-bed ion exchanger, moving-bed ion exchange device etc..
Film treatment facility is the separation of the different component utilizing the Selective Separation of film to realize feed liquid, purification, concentration, and what frequently involve in advanced treating is microfiltration, ultrafiltration, nanofiltration, and reverse osmosis.
Activated carbon adsorption facility, namely fills activated carbon in structures, utilizes the absorption property of activated carbon, remove the polluter in sewage.
Underload biochemical treatment facility refers to the biochemical treatment facility of dwell period growth, underrun.
Ozone oxidation facility is to make oxidant with ozone waste water is purified and disinfects.
The work process of this example is as follows:
The acid waste water that waterwater entrance is come in is after the acid waste water collecting pit in sewage collection module is collected, by the adjustment of pipeline valve, pH regulator submodule in waste water physicochemical processing module, module internal reflux pipe, coagulating sedimentation submodule, module internal reflux pipe and wet oxidation submodule process, waste water after process enters wastewater biochemical processing module, subsequently into the resin absorption submodule in Sewage advanced treatment module, the water after process reaches the discharge of one-level B standard.
Experimental data shows: after stable, and acid waste water pH value, by 1.0～2.0, is adjusted to about 7.0～7.2, and COD is reduced to about 50～80mg/L by 2000～3000mg/L.
The alkaline waste water that waterwater entrance is come in is after the alkaline waste water collecting pit in sewage collection module is collected, by the adjustment of pipeline valve, pH regulator submodule in waste water physicochemical processing module, module internal reflux pipe, coagulating sedimentation submodule, module internal reflux pipe and wet oxidation submodule process, waste water after process enters wastewater biochemical processing module, subsequently into the resin absorption submodule in Sewage advanced treatment module, the water after process reaches the discharge of one-level B standard.
Experimental data shows: after stable, and alkaline waste water pH value, by 13.0～14.0, is adjusted to about 7.0～7.2, and COD is reduced to about 50～80mg/L by 2000～3000mg/L.
Oils that waterwater entrance is come in, esters waste water are after the oils wastewater collection pond in sewage collection module is collected, by the adjustment of pipeline valve, air supporting submodule in waste water physicochemical processing module, module internal reflux pipe, coagulating sedimentation submodule, module internal reflux pipe, fenton aoxidize submodule, module internal reflux pipe, filter submodule, waste water after process delivers to wastewater biochemical processing module, puts through surmounting bank of tubes after up to standard.
Experimental data shows: after stable, and grease class Petroleum Wastewater material, by 100～150mg/L, is reduced to about 5～8mg/L, COD and is reduced to about 40～70mg/L by 2000～3000mg/L.
The benzene class waste water that waterwater entrance is come in is after the benzene class wastewater collection pond in sewage collection module is collected, by the adjustment of pipeline valve, after electrochemical oxidation submodule in waste water physicochemical processing module, send into wastewater biochemical processing module to process, enter back into the underload biochemical treatment submodule in Sewage advanced treatment module and after resin absorption submodule, qualified discharge.
Experimental data shows: after stable, and in waste water, COD is reduced to about 60～90mg/L by 2000～3000mg/L, and colourity, by about 200mg/L, is reduced to about 20～30mg/L.
The halohydrocarbon waste water that waterwater entrance is come in is after the halohydrocarbon wastewater collection pond in sewage collection module is collected, by the adjustment of pipeline valve, after coagulating sedimentation submodule in waste water physicochemical processing module, module internal reflux pipe, filtration submodule, module internal reflux pipe, Fenton oxidation submodule process, it is then fed into wastewater biochemical processing module, after the activated carbon adsorption resume module in Sewage advanced treatment module, qualified discharge.
Experimental data shows: after stable, and in waste water, COD is reduced to about 70～90mg/L by 2000～3000mg/L, and colourity, by 200～300mg/L, is reduced to about 20～30mg/L.
The heavy metal wastewater thereby that waterwater entrance is come in is after the heavy metal wastewater thereby collecting pit in sewage collection module is collected, by the adjustment of pipeline valve, after pH regulator submodule in waste water physicochemical processing module, module internal reflux pipe, coagulating sedimentation submodule, send into wastewater biochemical processing module, after entering back into the film process submodule process in Sewage advanced treatment module, qualified discharge.
Experimental data shows: after stable, and in waste water, COD is reduced to about 50～80mg/L, total Cd by 1～10mg/L by 2000～3000mg/L, is reduced to about 0.005～0.01mg/L, and total Cr, by 10～30mg/L, is reduced to about 0.05～0.1mg/L.
The Ammonia waste water that waterwater entrance is come in is after the amine wastewater collection pond in sewage collection module is collected, by the adjustment of pipeline valve, pH regulator submodule in waste water physicochemical processing module, module internal reflux pipe, stripping submodule, module internal reflux pipe, again through pH regulator submodule, module internal reflux pipe, be then passed through wet oxidation submodule after, after sending into the process of wastewater biochemical processing module, qualified discharge.
Experimental data shows: after stable, and in waste water, COD is reduced to about 50～80mg/L by 2000～3000mg/L, and ammonia nitrogen, by 100～300mg/L, is reduced to about 8～15mg/L.
Claims (6)
1. the modularized treatment system of a chemical packs barrelling cleaning waste water, it is made up of sewage collection module, waste water physicochemical processing module, wastewater biochemical processing module and Sewage advanced treatment module, it is characterized in that sewage collection module is connected with waste water physicochemical processing module, and be connected with wastewater biochemical processing module and Sewage advanced treatment module respectively by surmounting pipe；Sewage collection module is made up of wastewater collection pond group, and each wastewater collection pond in the group of wastewater collection pond is connected in parallel；Waste water physicochemical processing module is connected with wastewater biochemical processing module, and is connected with Sewage advanced treatment module or floss hole by surmounting pipe；Waste water physicochemical processing module is made up of materializing strategy submodule group, and each submodule in materializing strategy submodule group is connected in parallel, and module internal reflux pipe is connected with module inlet and module outlet respectively；Wastewater biochemical processing module is connected with Sewage advanced treatment module or is connected with floss hole by surmounting pipe；Wastewater biochemical processing module is made up of Aerobic Pond and anaerobic pond；Sewage advanced treatment module is connected with floss hole；Sewage advanced treatment module is made up of advanced treating submodule group, and each submodule in advanced treating submodule group is connected in parallel, and module internal reflux pipe is connected with module inlet and module outlet respectively.
2. the modularized treatment system of waste water is cleaned in chemical packs barrelling according to claim 1, it is characterised in that described wastewater collection pond group is made up of acid waste water collecting pit, alkaline waste water collecting pit, oils wastewater collection pond, esters wastewater collection pond, benzene class wastewater collection pond, halohydrocarbon wastewater collection pond, heavy metal wastewater thereby collecting pit, amine wastewater collection pond and standby pool.
3. the modularized treatment system of waste water is cleaned in chemical packs barrelling according to claim 1, it is characterised in that described materializing strategy submodule group is made up of pH regulator submodule, coagulating sedimentation submodule, air supporting submodule, filtration submodule, stripping submodule, sonochemical oxidation submodule, wet oxidation submodule, electrochemical oxidation submodule and Fenton oxidation submodule.
4. the modularized treatment system of waste water is cleaned in chemical packs barrelling according to claim 1, it is characterised in that described advanced treating submodule group is processed submodule, activated carbon adsorption submodule, electrochemical oxidation submodule, underload biochemical treatment submodule, ozone oxidation submodule and filtration submodule formed by resin absorption submodule, ion recon module, film.
5. the modularized treatment system of waste water is cleaned in chemical packs barrelling according to claim 3, it is characterized in that the pH regulator submodule in described materializing strategy submodule group is by mixed collection pond, pH regulator pond and intermediate pool are sequentially connected with composition, coagulating sedimentation submodule is by mixed collection pond, coagulating sedimentation facility and intermediate pool are sequentially connected with composition, air supporting submodule is by mixed collection pond, air supporting facility and intermediate pool are sequentially connected with composition, filter submodule by mixed collection pond, filtration facility and intermediate pool are sequentially connected with composition, stripping submodule is by mixed collection pond, stripping facility and intermediate pool are sequentially connected with composition；Sonochemical oxidation submodule is sequentially connected with is formed by mixed collection pond, sonochemical oxidation facility and intermediate pool；Wet oxidation submodule is sequentially connected with is formed by mixed collection pond, wet oxidation facility and intermediate pool；Electrochemical oxidation submodule is sequentially connected with is formed by mixed collection pond, electrochemical oxidation facility and intermediate pool；Fenton oxidation submodule is sequentially connected with is formed by mixed collection pond, Fenton oxidation facility and intermediate pool.
6. the modularized treatment system of waste water is cleaned in chemical packs barrelling according to claim 4, it is characterised in that the resin absorption submodule in described advanced treating submodule group is connected to form by mixed collection pond and resin absorption facility；Ion recon module is connected to form by mixed collection pond and ion commutating device；Film processes submodule and is connected to form by mixed collection pond and film treatment facility；Activated carbon adsorption submodule is connected to form by mixed collection pond and activated carbon adsorption facility；Electrochemical oxidation submodule is connected to form by mixed collection pond and electrochemical oxidation facility；Underload biochemical treatment submodule is connected to form by mixed collection pond and underload biochemical treatment facility；Ozone oxidation submodule is connected to form by mixed collection pond and ozone oxidation facility；Filter submodule to be connected to form by mixed collection pond and filtration facility.
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105439342A (en) * | 2016-01-11 | 2016-03-30 | 四川省环境保护科学研究院 | Modular processing system of chemical packing bucket cleaning wastewater |
| CN106881319A (en) * | 2017-01-19 | 2017-06-23 | 大连利丰包装有限公司 | The plastic box purging system and its method of work of a kind of sewage zero-discharge |
| CN108793558A (en) * | 2018-06-22 | 2018-11-13 | 浙江奇彩环境科技股份有限公司 | The processing method of phosphoric acid activation method Activated Carbon Production waste water |
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2016
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105439342A (en) * | 2016-01-11 | 2016-03-30 | 四川省环境保护科学研究院 | Modular processing system of chemical packing bucket cleaning wastewater |
| CN105439342B (en) * | 2016-01-11 | 2019-04-05 | 四川省环境保护科学研究院 | The modularized treatment system of chemical pail pack cleaning waste water |
| CN106881319A (en) * | 2017-01-19 | 2017-06-23 | 大连利丰包装有限公司 | The plastic box purging system and its method of work of a kind of sewage zero-discharge |
| CN106881319B (en) * | 2017-01-19 | 2019-03-29 | 大连利丰包装有限公司 | A kind of the plastic container cleaning system and its working method of sewage zero-discharge |
| CN108793558A (en) * | 2018-06-22 | 2018-11-13 | 浙江奇彩环境科技股份有限公司 | The processing method of phosphoric acid activation method Activated Carbon Production waste water |
| CN108793558B (en) * | 2018-06-22 | 2021-04-27 | 浙江奇彩环境科技股份有限公司 | Method for treating wastewater generated in activated carbon production by phosphoric acid activation method |
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