CN205061793U - A sewage treatment system for diosmi production - Google Patents
A sewage treatment system for diosmi production Download PDFInfo
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- CN205061793U CN205061793U CN201520692785.3U CN201520692785U CN205061793U CN 205061793 U CN205061793 U CN 205061793U CN 201520692785 U CN201520692785 U CN 201520692785U CN 205061793 U CN205061793 U CN 205061793U
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- iodine
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Abstract
The embodiment of the utility model discloses a sewage treatment system for diosmi production, this sewage treatment system includes: useless iodine recovery system connects the production system to including the waste liquid export, useless iodine recovery system's waste liquid export is connected to technology waste water equalizing basin, transfer the acid tank, joining technology waste water equalizing basin, micro electrolytic reactor connects and transfers the acid tank, micro electrolytic reactor is connected to the neutralizing tank, the neutralizing tank is connected to first sedimentation tank, first sedimentation tank is connected in the anaerobism pond, the anaerobism pond is connected to the second sedimentation tank, sludge tihckener connects the second sedimentation tank, sludge tihckener is connected to box compressor. The utility model discloses a sewage treatment system for diosmi production can be with the direct recovery of iodine of giving up to emission standard is synthesized to the sewage that reaches the national requirements after handling.
Description
Technical field
The utility model relates to a kind of chemical agent producing apparatus, particularly relates to a kind of Sewage treatment systems of producing for diosmin.
Background technology
Diosmin has another name called S 5682, English name: Diosmin, molecular formula: C28H32O15, molecular weight: 608.54, chemical name: Diosmin; 7-{ [6-O-(6-deoxidation-α-L-seminose)-β-D-Glucopyranose] oxygen base }-5-hydroxyl-2-(3-hydroxyl-4-anisole)-4H-L-benzopyran-4-one, diosmin is a kind of flavonoid medicine, its suitability for industrialized production is with the hesperidine extracted from the natural dried immature fruit of citron orange for raw material, through semi-synthetic.
In the process of producing diosmin, the sewage that produces is mainly the washes washed material and produce, and main component is sodium-acetate, sodium-chlor, potassium sulfate etc., also has part material to decompose the organism produced, and methyl alcohol vinasse and contain iodine 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.Further, the iodine in iodine waste liquid directly emits also can cost of idleness.
Utility model content
The utility model embodiment technical problem to be solved is to provide a kind of Sewage treatment systems of producing for diosmin, to solve in prior art discharging of waste liquid not environmentally and the problem of iodine waste.
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 comprises: useless iodine recovery system, connects production system, and comprise waste liquid outlet; Processing wastewater equalizing tank, connects the waste liquid outlet of useless iodine recovery system; Acid adjustment groove, Joining Technology wastewater equalization pond; Micro-electrolysis reactor, connects acid adjustment groove; Neutralizing well, connects micro-electrolysis reactor; First settling tank, connects neutralizing well; Anaerobic pond, connects the first settling tank; Second settling tank, connects anaerobic pond; Sludge thickener, connects the second settling tank; Box compressor, connects sludge thickener.
Wherein, useless iodine recovery system comprises: iodine waste liquid leaves standstill tank, connects the production system of diosmin; Photochemical reactor, connects iodine waste liquid and leaves standstill tank; Iodine waste liquid souring tank, connects photochemical reactor by the first plate filter; Reaction precipitation tank, connects iodine waste liquid souring tank by the second plate filter; Whizzer, ligation setting tank, and in whizzer, be provided with filter cloth and waste liquid outlet, iodine remains on filter cloth, and waste liquid flow to processing wastewater equalizing tank by waste liquid outlet.
Wherein, box compressor Joining Technology wastewater equalization pond, the wastewater streams that box compressor produces is to processing wastewater equalizing tank.
Wherein, sludge pump is provided with between the second settling tank and sludge thickener.
Wherein, spiral pump is provided with between sludge thickener and box compressor.
Implement the utility model embodiment, there is following beneficial effect: useless iodine can directly reclaim by the Sewage treatment systems for diosmin production of the present utility model, and reaches the integrated wastewater discharge standard of national requirements after treatment.
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 first embodiment of the Sewage treatment systems for diosmin production that the utility model provides;
Fig. 2 is the structural representation of the useless iodine recovery system in Fig. 1.
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 first embodiment of the Sewage treatment systems for diosmin production that the utility model provides.In the present embodiment, Sewage treatment systems comprises useless iodine recovery system 10, processing wastewater equalizing tank 20, acid adjustment groove 30, micro-electrolysis reactor 40, neutralizing well 50, first settling tank 61, anaerobic pond 70, second settling tank 62, sludge thickener 80 and box compressor 90.
Useless iodine recovery system connects production system, and comprises waste liquid outlet.It is please the structural representation of the useless iodine recovery system in Fig. 1 with further reference to Fig. 2, Fig. 2.In the present embodiment, iodine recovery system 10 of giving up comprises iodine waste liquid and leaves standstill tank 11, photochemical reactor 12, iodine waste liquid souring tank 13, reaction precipitation tank 14, whizzer 15, sulphur acid meter measuring tank 16 and hydrogen peroxide hold-up vessel 17.
Iodine waste liquid leaves standstill the production system that tank 11 connects diosmin.Photochemical reactor 12 connects iodine waste liquid by iodine waste drains pump and leaves standstill tank 11.Iodine waste liquid souring tank 13 connects photochemical reactor 12 by the first plate filter.Reaction precipitation tank 14 connects iodine waste liquid souring tank 13 by the second plate filter.Whizzer 15 ligation setting tank 14.Sulphur acid meter measuring tank 16 connects iodine waste liquid souring tank 13, thinks that iodine waste liquid souring tank 13 provides sulfuric acid.Hydrogen peroxide hold-up vessel 17 ligation setting tank 14 and photochemical reactor 12, think that reaction precipitation tank 14 and photochemical reactor 12 provide hydrogen peroxide.
Adopt said system, what produce in production system first delivers to iodine waste liquid leave standstill tank 11 containing iodine waste liquid, then enters photochemical reactor 12 and carries out and reaction, then be delivered to iodine waste liquid souring tank 13 by the first plate filter, slowly add sulfuric acid and stir; Deliver to reaction precipitation tank 14 by the second plate filter again, slowly add hydrogen peroxide and place some hours, finally throw away liquid with whizzer 15 filtration and enter processing wastewater equalizing tank 2020 by waste liquid outlet, the iodine be recycled in filter cloth.Preferably, by sulfuric acid transferpump and hydrogen peroxide transferpump, barreled raw material is carried respectively in sulphur acid meter measuring tank 16 and hydrogen peroxide hold-up vessel 17.
Processing wastewater equalizing tank 20 connects the waste liquid outlet of useless iodine recovery system 10.Acid adjustment groove 30 Joining Technology wastewater equalization pond 20.Micro-electrolysis reactor 40 connects acid adjustment groove 30.Neutralizing well 50 connects micro-electrolysis reactor 40.First settling tank 61 connects neutralizing well 50.Anaerobic pond 70 connects the first settling tank 61.Second settling tank 62 connects anaerobic pond 70.Sludge thickener 80 connects the second settling tank 62.Box compressor 90 connects sludge thickener 80.
Preferably, box compressor 90 Joining Technology wastewater equalization pond 20, the wastewater streams that box compressor 90 produces is to processing wastewater equalizing tank 20.Sludge pump is provided with between second settling tank 62 and sludge thickener 80.Spiral pump is provided with between sludge thickener 80 and box compressor 90.
The sewage discharged in production system comprises processing wastewater and iodine waste liquid, and iodine waste liquid enters after useless iodine recovery system 10 carries out useless iodine recovery and enters processing wastewater equalizing tank 20, and processing wastewater is directly discharged into processing wastewater equalizing tank 20.Waste water in processing wastewater equalizing tank 20 squeezes into acid adjustment groove 30 through pump, adds after sulfuric acid reduces pH value from flowing to micro-electrolysis reactor 40.Add sodium hydroxide carry out neutralization reaction from flowing to neutralizing well 50 after microelectrolysis processing, neutralizing well 50 water outlet precipitates from flowing to settling tank, settling tank water outlet, from flowing to anaerobic pond 70 (now can mix with sanitary sewage), enters the biochemical treatment stage.After the anaerobic effect of anaerobic pond 70 and the good of contact-oxidation pool support effect, water outlet enters sedimentation in secondary sedimentation tank clarification, gets final product qualified discharge.The mud of settling tank and second pond is regularly squeezed into sludge thickener 80 by sludge pump and is concentrated, and thickened sludge squeezes into chamber filter press press filtration through spiral pump.Filtrate is back to sludge thickener 80, and sanitary landfill is carried out in dewatered sludge outward transport.The supernatant liquor of sludge thickener 80 is back to processing wastewater equalizing tank 20, proceeds circulation.
Implement the utility model embodiment, there is following beneficial effect: useless iodine can directly reclaim by the Sewage treatment systems for diosmin production of the present utility model, and reaches the integrated wastewater discharge standard of national requirements after treatment.
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 (5)
1. for the Sewage treatment systems that diosmin is produced, it is characterized in that, the described Sewage treatment systems for diosmin production comprises:
Useless iodine recovery system, connects production system, and comprises waste liquid outlet;
Processing wastewater equalizing tank, connects the waste liquid outlet of useless iodine recovery system;
Acid adjustment groove, connects described processing wastewater equalizing tank;
Micro-electrolysis reactor, connects described acid adjustment groove;
Neutralizing well, connects described micro-electrolysis reactor;
First settling tank, connects described neutralizing well;
Anaerobic pond, connects described first settling tank;
Second settling tank, connects described anaerobic pond;
Sludge thickener, connects described second settling tank;
Box compressor, connects described sludge thickener.
2. Sewage treatment systems of producing for diosmin according to claim 1, it is characterized in that, described useless iodine recovery system comprises:
Iodine waste liquid leaves standstill tank, connects the production system of diosmin;
Photochemical reactor, connects described iodine waste liquid and leaves standstill tank;
Iodine waste liquid souring tank, connects described photochemical reactor by the first plate filter;
Reaction precipitation tank, connects described iodine waste liquid souring tank by the second plate filter;
Whizzer, connects described reaction precipitation tank, and is provided with filter cloth and waste liquid outlet in described whizzer, and iodine remains on described filter cloth, and waste liquid flow to described processing wastewater equalizing tank by waste liquid outlet.
3. Sewage treatment systems of producing for diosmin according to claim 1, it is characterized in that, described box compressor connects described processing wastewater equalizing tank, and the wastewater streams that described box compressor produces is to described processing wastewater equalizing tank.
4. Sewage treatment systems of producing for diosmin according to claim 1, is characterized in that, be provided with sludge pump between described second settling tank and described sludge thickener.
5. Sewage treatment systems of producing for diosmin according to claim 4, is characterized in that, be provided with spiral pump between described sludge thickener and described box compressor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520692785.3U CN205061793U (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 |
|---|---|---|---|
| CN201520692785.3U CN205061793U (en) | 2015-09-09 | 2015-09-09 | A sewage treatment system for diosmi production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205061793U true CN205061793U (en) | 2016-03-02 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520692785.3U Expired - Fee Related CN205061793U (en) | 2015-09-09 | 2015-09-09 | A sewage treatment system for diosmi production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205061793U (en) |
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2015
- 2015-09-09 CN CN201520692785.3U patent/CN205061793U/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. |
|
| 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 |