CN205061794U - A sewage treatment system for diosmi production - Google Patents
A sewage treatment system for diosmi production Download PDFInfo
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- CN205061794U CN205061794U CN201520692810.8U CN201520692810U CN205061794U CN 205061794 U CN205061794 U CN 205061794U CN 201520692810 U CN201520692810 U CN 201520692810U CN 205061794 U CN205061794 U CN 205061794U
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- sewage treatment
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- sewage
- treatment systems
- diosmin
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Abstract
The embodiment of the utility model discloses a sewage treatment system for diosmi production, this a sewage treatment system for diosmi production include the sewage import, iodine waste liquid collecting pit is with the sewage access connection, the photochemical reaction ware is connected with iodine waste liquid collecting pit, wherein is provided with the ultraviolet lamp, technology waste water equalizing basin is connected with the photochemical reaction ware, transfer the acid tank, be connected with technology waste water equalizing basin, micro electrolytic reactor is connected with transferring the acid tank, the neutralizing tank is connected with micro electrolytic reactor, the sedimentation tank is connected with the neutralizing tank, ABR anaerobism pond is connected with the sedimentation tank, contact oxidation tank is connected with ABR anaerobism pond, two sedimentation tanks are connected with contact oxidation tank, the discharge port is connected with two sedimentation tanks. The utility model discloses a sewage treatment system for diosmi production carries out sewage treatment to exhaust sewage characteristics behind the producing area ao siming, simple structure, and the sewage after the processing can reach national sewage and synthesize emission standard.
Description
Technical field
The utility model relates to a kind of Sewage treatment systems, particularly relates to a kind of Sewage treatment systems of producing for diosmin.
Background technology
Diosmin is-kind of flavonoid medicine, has the effect of vitamin P sample, can reduce the permeability of vascular fragility and exception, and again for preventing and treating hypertension and arteriosclerotic assisting therapy, therefore, the market requirement is larger.Can produce a large amount of sewage in the process of producing diosmin, be mainly the washes washed material and produce, composition is sodium-acetate, sodium-chlor, potassium sulfate etc., also has part material to decompose the organism produced, and methyl alcohol vinasse and iodine Recycling of waste liquid etc.Sewage belongs to high concentrated organic wastewater, and raw sewerage can not reach national sewage comprehensive emission standard, if directly discharged, can produce shock effect, and damage external aqueous environment the influent quality of public sewage disposal appts.
Utility model content
The utility model embodiment technical problem to be solved is, does not reach the problem of national sewage comprehensive emission standard for the sewage of discharging in diosmin production process, proposes a kind of Sewage treatment systems of producing for diosmin.
In order to solve the problems of the technologies described above, the utility model embodiment provides a kind of Sewage treatment systems of producing for diosmin, and this Sewage treatment systems being used for diosmin production comprises: wastewater inlet; Iodine waste collection pond, is connected with wastewater inlet, for collecting the iodine waste liquid in sewage; Photochemical reactor, is connected with iodine waste collection pond, is provided with ultraviolet lamp in photochemical reactor, for providing UV-irradiation when iodine waste liquid carries out photochemical reaction, makes it produce photochemical reaction; Processing wastewater equalizing tank, is connected with photochemical reactor; Acid adjustment groove, is connected with processing wastewater equalizing tank, for regulating the pH value of the waste water flowed out from processing wastewater equalizing tank; Micro-electrolysis reactor, is connected with acid adjustment groove, and the waste water in acid adjustment groove carries out microelectrolysis processing from flowing in micro-electrolysis reactor; Neutralizing well, is connected with micro-electrolysis reactor, and the waste water in micro-electrolysis reactor carries out neutralization reaction from flowing in neutralizing well; Settling tank, is connected with neutralizing well; ABR anaerobic pond, is connected with settling tank, and the waste water in settling tank carries out anaerobic reaction from flowing in ABR anaerobic pond; Contact-oxidation pool, is connected with ABR anaerobic pond, carries out carrying out oxygen consumption reaction in the inflow of the waste water after anaerobic reaction contact-oxidation pool; Two settling tanks, are connected with contact-oxidation pool; Discharge outlet, is connected with two settling tanks.
Wherein, the Sewage treatment systems of producing for diosmin comprises iodine liquid lift pump further, is arranged between iodine waste collection pond and photochemical reactor, for being squeezed in photochemical reactor by iodine waste liquid.
Wherein, water pump is provided with between processing wastewater equalizing tank and acid adjustment groove.
Wherein, the Sewage treatment systems of producing for diosmin comprises sludge thickener further, and sludge thickener is connected with settling tank and two settling tanks respectively, for the concentrated mud flowed out from settling tank and two settling tanks.
Wherein, the first sludge pump is provided with between settling tank and sludge thickener.
Wherein, the second sludge pump is provided with between two settling tanks and sludge thickener.
Implement the utility model embodiment, there is following beneficial effect: the Sewage treatment systems for diosmin production of the present utility model carries out sewage disposal for the sewage feature of discharging after production diosmin, structure is simple, and the sewage after process can reach national sewage comprehensive emission standard.
Accompanying drawing explanation
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, be briefly described to the accompanying drawing used required in embodiment or description of the prior art below, apparently, accompanying drawing in the following describes is only embodiments more of the present utility model, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Fig. 1 is the structural representation of the Sewage treatment systems for diosmin production that the utility model provides.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, be clearly and completely described the technical scheme in the utility model embodiment, obviously, described embodiment is only the utility model part embodiment, instead of whole embodiments.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
Refer to Fig. 1, Fig. 1 is the structural representation of the Sewage treatment systems for diosmin production that the utility model provides.This Sewage treatment systems being used for diosmin production comprises wastewater inlet 10, iodine waste collection pond 11, photochemical reactor 12, processing wastewater equalizing tank 13, acid adjustment groove 14, micro-electrolysis reactor 15, neutralizing well 16, settling tank 17, ABR anaerobic pond 18, contact-oxidation pool 19, two settling tank 20, sludge thickener 21 and discharge outlet 22.
Iodine waste collection pond 11 is connected with wastewater inlet 10, for collecting the iodine waste liquid in sewage.Photochemical reactor 12 is connected with iodine waste collection pond 11, is provided with ultraviolet lamp (not shown) in photochemical reactor 12, for providing UV-irradiation when iodine waste liquid carries out photochemical reaction, makes it produce photochemical reaction.Iodine liquid lift pump (not shown) is arranged between iodine waste collection pond 11 and photochemical reactor 12, for being squeezed in photochemical reactor 12 by iodine waste liquid.
Processing wastewater equalizing tank 13 is connected with photochemical reactor 12.Acid adjustment groove 14 is connected with processing wastewater equalizing tank 13, for regulating the pH value of the waste water flowed out from processing wastewater equalizing tank 13.Waste water in processing wastewater equalizing tank 13 is driven in acid adjustment groove 14 by water pump (not shown).Micro-electrolysis reactor 15 is connected with acid adjustment groove 14, and the waste water in acid adjustment groove 14 carries out microelectrolysis processing from flowing in micro-electrolysis reactor 15.
Neutralizing well 16 is connected with micro-electrolysis reactor 15, and the waste water in micro-electrolysis reactor 15 carries out neutralization reaction from flowing in neutralizing well 16.Settling tank 17 is connected with neutralizing well 16.ABR (AnaerobicBaffledReactor, anaerobism flap reactor) anaerobic pond 18 is connected with settling tank 17, and the waste water in settling tank 17 carries out anaerobic reaction from flowing in ABR anaerobic pond 18.
Contact-oxidation pool 19 is connected with ABR anaerobic pond 18, carries out carrying out oxygen consumption reaction in the inflow of the waste water after anaerobic reaction contact-oxidation pool 19.Two settling tanks 20 are connected with contact-oxidation pool 19.Discharge outlet 22 is connected with two settling tanks 20.Sludge thickener 21 is connected with settling tank 17 and two settling tanks 20 respectively, for the concentrated mud flowed out from settling tank 17 and two settling tanks 20.Be provided with the first sludge pump (not shown) between settling tank 17 and sludge thickener 21, between two settling tanks 20 and sludge thickener 21, be provided with the second sludge pump (not shown).
Sewage flows into Sewage treatment systems by wastewater inlet 10, and the iodine waste liquid in sewage is collected by iodine waste collection pond 11, squeezes in photochemical reactor 12, carry out pre-treatment through iodine liquid lift pump.Iodine waste liquid in photochemical reactor 12 produces photochemical reaction under the strong illumination of ultraviolet lamp, waste water after process enters processing wastewater equalizing tank 13 and mixes with processing wastewater, composite waste in processing wastewater equalizing tank 13 squeezes into acid adjustment groove 14 through water pump, add the pH value of sulfuric acid reduction waste water in acid adjustment groove 14 after, waste water is from flowing to micro-electrolysis reactor 15.From flowing to neutralizing well 16 after microelectrolysis processing, sodium hydroxide is added and waste water carries out neutralization reaction in neutralizing well 16, waste water after neutralization precipitates from flowing to settling tank 17, settling tank 17 water outlet is from flowing in ABR anaerobic pond 18, mix with the sanitary sewage in ABR anaerobic pond 18, there is anaerobic reaction, ABR anaerobic pond 18 water outlet is from flowing to contact-oxidation pool 19, carry out oxygen consumption reaction, water outlet subsequently enters second pond 20 and carries out precipitation clarification, and the water after clarification can enter discharge outlet 22 qualified discharge.The mud of settling tank 17 and two settling tanks 20 by sludge pump regularly squeeze into sludge thickener 21 carry out concentrated after transport and carry out sanitary landfill.
The present embodiment is preferred embodiment, in other embodiments, can modify according to practical situation, as arranged a sludge thickener 21 respectively at settling tank 17 and two settling tanks 20 side, carries out sludge condensation respectively.
Implement the utility model embodiment, there is following beneficial effect: the Sewage treatment systems for diosmin production of the present utility model carries out sewage disposal for the sewage feature of discharging after production diosmin, structure is simple, and the sewage after process can reach national sewage comprehensive emission standard.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (6)
1. for the Sewage treatment systems that diosmin is produced, it is characterized in that, the described Sewage treatment systems for diosmin production comprises:
Wastewater inlet;
Iodine waste collection pond, is connected with described wastewater inlet, for collecting the iodine waste liquid in sewage;
Photochemical reactor, is connected with described iodine waste collection pond, is provided with ultraviolet lamp in described photochemical reactor, for providing UV-irradiation when described iodine waste liquid carries out photochemical reaction;
Processing wastewater equalizing tank, is connected with described photochemical reactor;
Acid adjustment groove, is connected with described processing wastewater equalizing tank, for regulating the pH value of the waste water flowed out from described processing wastewater equalizing tank;
Micro-electrolysis reactor, is connected with described acid adjustment groove, and the waste water in described acid adjustment groove carries out microelectrolysis processing from flowing in described micro-electrolysis reactor;
Neutralizing well, is connected with described micro-electrolysis reactor, and the waste water in described micro-electrolysis reactor carries out neutralization reaction from flowing in described neutralizing well;
Settling tank, is connected with described neutralizing well;
ABR anaerobic pond, is connected with described settling tank, and the waste water in described settling tank carries out anaerobic reaction from flowing in described ABR anaerobic pond;
Contact-oxidation pool, is connected with described ABR anaerobic pond, and the waste water carried out after anaerobic reaction flows in described contact-oxidation pool and carries out oxygen consumption reaction;
Two settling tanks, are connected with described contact-oxidation pool;
Discharge outlet, is connected with described two settling tanks.
2. Sewage treatment systems of producing for diosmin according to claim 1, it is characterized in that, the described Sewage treatment systems for diosmin production comprises iodine liquid lift pump further, be arranged between described iodine waste collection pond and described photochemical reactor, for described iodine waste liquid is squeezed in described photochemical reactor.
3. Sewage treatment systems of producing for diosmin according to claim 1, is characterized in that, be provided with water pump between described processing wastewater equalizing tank and described acid adjustment groove.
4. Sewage treatment systems of producing for diosmin according to claim 1, it is characterized in that, the described Sewage treatment systems for diosmin production comprises sludge thickener further, described sludge thickener is connected with described settling tank and described two settling tanks respectively, for the concentrated mud flowed out from described settling tank and described two settling tanks.
5. Sewage treatment systems of producing for diosmin according to claim 4, is characterized in that, be provided with the first sludge pump between described settling tank and described sludge thickener.
6. Sewage treatment systems of producing for diosmin according to claim 4, is characterized in that, be provided with the second sludge pump between described two settling tanks and described sludge thickener.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520692810.8U CN205061794U (en) | 2015-09-09 | 2015-09-09 | A sewage treatment system for diosmi production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520692810.8U CN205061794U (en) | 2015-09-09 | 2015-09-09 | A sewage treatment system for diosmi production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205061794U true CN205061794U (en) | 2016-03-02 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520692810.8U Expired - Fee Related CN205061794U (en) | 2015-09-09 | 2015-09-09 | A sewage treatment system for diosmi production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205061794U (en) |
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2015
- 2015-09-09 CN CN201520692810.8U patent/CN205061794U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 445311 Four Groups of Longli Village, Changliang Township, Jianshi County, Enshi Tujia and Miao Autonomous Prefecture, Hubei Province Patentee after: Hubei Yuantong Bioengineering Co., Ltd. Address before: 445311 Four Groups of Longli Village, Changliang Township, Jianshi County, Enshi Tujia and Miao Autonomous Prefecture, Hubei Province Patentee before: JIANSHI YUANTONG BIOLOGICAL ENGINEERING CO., LTD. |
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| 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: 20160302 Termination date: 20200909 |