CN205188076U - Effluent disposal system of cosmetics production - Google Patents
Effluent disposal system of cosmetics production Download PDFInfo
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- CN205188076U CN205188076U CN201520952404.0U CN201520952404U CN205188076U CN 205188076 U CN205188076 U CN 205188076U CN 201520952404 U CN201520952404 U CN 201520952404U CN 205188076 U CN205188076 U CN 205188076U
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Abstract
The utility model discloses an effluent disposal system of cosmetics production, include the homogenization equalizing basin, grid pond, air supporting pond, coagulating sedimentation tank, anaerobism pond, the good oxygen pond that connect gradually through the pipeline, the good external outer discharge pipe in oxygen pond, the homogenization equalizing basin carries out the homogenization to be adjusted, grid pond check remove granule solid and floater among the cosmetics waste water, coagulating sedimentation tank gets rid of suspension solids and surface -activeagent and organic matter in the waste water, the anaerobism pond is to pressing oxygen biodegradable, the micro molecule organic matter degradation of good oxygen pond in with waste water is water, carbon dioxide and inorganic salts. This is novel to carry out the continuous processing to cosmetics waste water, provides convenience for the waste water treatment of cosmetics enterprises.
Description
Technical field
The utility model relates to cosmetics production preparing technical field, relates in particular to a kind of Waste Water Treatment of cosmetics production.
Background technology
" national environmental protection Eleventh Five-Year Plan " (hereinafter referred to as " planning ") is pointed out: current, the contradiction that China's socio-economic development and resource environment retrain, and environment protection is faced with formidable challenges.Each department, all departments must deeply implement the Scientific Outlook on Development, Economic Development Mode Conversion, make great efforts and solve the healthy outstanding environmental problem with affecting the sustainable development of socio-economy of the harm people, make great efforts built environment friendly society.Tightly around the total emissions of major pollutants control objectives that realization " planning " is determined, using preventing and remedying pollution as the most important thing, to accelerate restructuring, strengthen pollution control.
According to " planning " requirement, disposal of pollutants overall control is carried out in recent years one after another in various places.Environmental administration carries out tracking investigation to contaminating enterprises' blowdown flow rate, water intaking chemical examination, and the enterprise large to blowdown flow rate orders and carry out environment treating facility rectification, fails the enterprise of meet the requirement of environmental protection to ban in accordance with the law.Cosmetics production industry is one of key object of monitoring of environment all the time.The control of blowdown flow rate makes cosmetics industrial enterprise add extra cost, also limit the industrial scale of enterprise simultaneously.Cosmetics industrial enterprise will under existing production technique and condition expanding production amount, just must carry out control polluted articles quantity discharged by improving environmental protection treatment efficiency.
Cosmetic-producing wastewater complicated component, containing kinds of surface promoting agent, auxiliary agent and pigment.Its Main Components has: the various surfactants such as alkyl polyoxyethylene sulfates R-CH20, wetting Agent for Printing Inks, buider, pigment AES etc.Waste water COD is high, lathering property is strong, change of water quality is large.A large amount of foams that tensio-active agent in this type of waste water causes are difficult points in administering.In addition, a large amount of foams of waste water owing to being formed when pneumatic stirring or biochemical aeration in treating processes, not only increase the difficulty of operation, also can reduce the processing efficiency of waste water significantly simultaneously.Therefore, effective process of cosmetic-producing wastewater is the difficult problem that environmental pollution administers field always.
Utility model content
The purpose of this utility model is the defect for above-mentioned prior art, provides a kind of Waste Water Treatment of cosmetics production, solves the difficult problem that makeup environmental pollution administers field.
To achieve these goals, the technical solution of the utility model is:
A Waste Water Treatment for cosmetics production, comprises the homogenizing equalizing tank, grating tank, air flotation pool, coagulative precipitation tank, anaerobic pond, the Aerobic Pond that are connected successively by pipeline, the external outer comb of described Aerobic Pond;
Described homogenizing equalizing tank flows into waste water that different cosmetics production workshop produces and carries out homogenizing adjustment, improves the handlability of waste water, reduces issuablely in biochemical treatment process to go out load;
Described grating tank lattice are except the granular solids in cosmetic-producing wastewater and floating matter, and the front of grating tank vertically arranges coarse rack, cross except macrobead solid and floating matter; The tilting fine fack in back, filters slightly little granular solids and floating matter;
Described air flotation pool, comprise be connected with outside sewage water inlet pipe air flotation pool exposure chamber, release room, gas-floating chamber, dissolved air water storage chamber, mud room, the leveling board making sewage repeatedly be folded to flowing is provided with in described air flotation pool exposure chamber, air flotation pool exposure chamber be provided with vertical partition wall between release room, the bottom of described vertical partition wall is provided with the connected entrance that air flotation pool exposure chamber is connected with release room; The first sloping core is provided with between described release room and gas-floating chamber, described release room is communicated with gas-floating chamber top, described dissolved air water storage chamber is positioned at the below of mud room, centre is separated by dividing plate, be provided with flap between described gas-floating chamber and dissolved air water storage chamber, mud room, described flap is arranged with the connected entrance that gas-floating chamber is communicated with dissolved air water storage chamber; Described gas-floating chamber upper end is provided with slag scraper;
Described coagulative precipitation tank removes suspended solid thing in waste water and tensio-active agent and organism, and described coagulative precipitation tank is circumscribed with chemicals dosing plant;
Described anaerobic pond, to the biological degradation of pressure oxygen, is provided with the cleaning microporous aeration disc in pond and the sludge stirring machine for stirring double oxygen mud in anaerobic pond;
Small organic molecule in waste water is degraded to water, carbonic acid gas and inorganic salt by described Aerobic Pond, and the bottom even of Aerobic Pond is covered with as bacteria metabolism provides the microporous aeration disc of required dissolved oxygen.
As the improvement to technique scheme, described coagulative precipitation tank and the external sludge thickener of anaerobic pond, described sludge thickener connects pressure filter.
Compared with prior art, the beneficial effects of the utility model are:
The Waste Water Treatment of cosmetics production of the present utility model, the waste water that different cosmetics production workshop produces is incorporated in homogenizing equalizing tank, carry out homogenizing adjustment, when preventing the waste water quality change that produces because of different workshop excessive once again, adverse influence is caused to sewage treatment equipment; Homogenizing equalizing tank carries out homogenizing adjustment according to the change of water quality and quantity, improves the handlability of waste water, reduces issuablely in biochemical treatment process to go out load;
In grating tank, grid is set, removes the macrobead solid in cosmetic-producing wastewater and floating matter, ensure the normal dynamic row of subsequent disposal facility; Coarse rack, fine fack make this process gradation sense strong;
Air flotation pool can be removed a large amount of mineral suspensions such as talcum powder, mica powder in cosmetic-producing wastewater; Under the effect of coagulation dosage and coagulant aids, the suspended substance that particle can be made tiny forms larger particle flocculation body, then removes through air supporting;
The hydrolysis reaction of anaerobic pond, can make the larger molecular organics of difficult degradation in waste water change the small organic molecule of easily degraded into, improve the biodegradability of waste water, remove most LAS simultaneously;
Waste water through anaerobic treatment enters Aerobic Pond, and under the effect of aerobic microbiological, small organic molecule is degraded to water, carbonic acid gas and inorganic salt, and the organism in waste water is removed further, and supernatant liquor can directly discharge through outer comb.
The mud that the viscosity that coagulative precipitation tank, anaerobic pond produce is higher enters in sludge thickener concentrated, then becomes outer dynamic after mud cake through pressure filter press filtration, can be used as fertilizer and uses.
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 structural representation of the present utility model.
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; any amendment of doing, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
As shown in Figure 1, the Waste Water Treatment of cosmetics production of the present utility model, comprises the homogenizing equalizing tank 1, grating tank 2, air flotation pool 3, coagulative precipitation tank 4, anaerobic pond 5, the Aerobic Pond 6 that are connected successively by pipeline, the external outer comb of described Aerobic Pond 6;
Described homogenizing equalizing tank 1 flows into waste water that different cosmetics production workshop produces and carries out homogenizing adjustment, improves the handlability of waste water, reduces issuablely in biochemical treatment process to go out load;
Described grating tank 2 lattice are except the granular solids in cosmetic-producing wastewater and floating matter, and the front of grating tank vertically arranges coarse rack 7, cross except macrobead solid and floating matter; The tilting fine fack 8 in back, filters slightly little granular solids and floating matter;
Described air flotation pool 3, comprise be connected with outside sewage water inlet pipe air flotation pool exposure chamber 9, release room 10, gas-floating chamber 11, dissolved air water storage chamber 12, mud room 13, the leveling board 14 making sewage repeatedly be folded to flowing is provided with in described air flotation pool exposure chamber 9, be provided with vertical partition wall between air flotation pool exposure chamber 9 with release room 10, the bottom of described vertical partition wall is provided with the connected entrance that air flotation pool exposure chamber 9 is connected with release room 10; The first sloping core 15 is provided with between described release room 10 and gas-floating chamber 11, described release room 10 is communicated with gas-floating chamber 11 top, described dissolved air water storage chamber 12 is positioned at the below of mud room 13, centre is separated by dividing plate, be provided with flap between described gas-floating chamber 11 and dissolved air water storage chamber 12, mud room 13, described flap is arranged with the connected entrance that gas-floating chamber 11 is communicated with dissolved air water storage chamber 12; Described gas-floating chamber 11 upper end is provided with slag scraper 16;
Described coagulative precipitation tank 4 removes suspended solid thing in waste water and tensio-active agent and organism, and described coagulative precipitation tank 4 is circumscribed with chemicals dosing plant 17;
Described anaerobic pond 5, to the biological degradation of pressure oxygen, is provided with the cleaning microporous aeration disc in pond and the sludge stirring machine for stirring double oxygen mud in anaerobic pond 5;
Small organic molecule in waste water is degraded to water, carbonic acid gas and inorganic salt by described Aerobic Pond 6, and the bottom even of Aerobic Pond 6 is covered with as bacteria metabolism provides the microporous aeration disc of required dissolved oxygen.
Described coagulative precipitation tank 4 and the external sludge thickener 18 of anaerobic pond 5, described sludge thickener 18 connects pressure filter 19.
The Waste Water Treatment of cosmetics production of the present utility model, the waste water that different cosmetics production workshop produces is incorporated in homogenizing equalizing tank, carry out homogenizing adjustment, when preventing the waste water quality change that produces because of different workshop excessive once again, adverse influence is caused to sewage treatment equipment; Homogenizing equalizing tank carries out homogenizing adjustment according to the change of water quality and quantity, improves the handlability of waste water, reduces issuablely in biochemical treatment process to go out load;
In grating tank, grid is set, removes the macrobead solid in cosmetic-producing wastewater and floating matter, ensure the normal dynamic row of subsequent disposal facility; Coarse rack, fine fack make this process gradation sense strong;
Air flotation pool can be removed a large amount of mineral suspensions such as talcum powder, mica powder in cosmetic-producing wastewater; Under the effect of coagulation dosage and coagulant aids, the suspended substance that particle can be made tiny forms larger particle flocculation body, then removes through air supporting;
The hydrolysis reaction of anaerobic pond, can make the larger molecular organics of difficult degradation in waste water change the small organic molecule of easily degraded into, improve the biodegradability of waste water, remove most LAS simultaneously;
Waste water through anaerobic treatment enters Aerobic Pond, and under the effect of aerobic microbiological, small organic molecule is degraded to water, carbonic acid gas and inorganic salt, and the organism in waste water is removed further, and supernatant liquor can directly discharge through outer comb.
The mud that the viscosity that coagulative precipitation tank, anaerobic pond produce is higher enters in sludge thickener concentrated, then becomes outer dynamic after mud cake through pressure filter press filtration, can be used as fertilizer and uses.
The above is only a kind of embodiment of the present utility model; it should be pointed out that for those skilled in the art, under the prerequisite not departing from the utility model know-why; can also make some improvement, these improvement also should be considered as protection domain of the present utility model.
Claims (2)
1. a Waste Water Treatment for cosmetics production, is characterized in that: comprise the homogenizing equalizing tank, grating tank, air flotation pool, coagulative precipitation tank, anaerobic pond, the Aerobic Pond that are connected successively by pipeline, the external outer comb of described Aerobic Pond;
Described homogenizing equalizing tank flows into waste water that different cosmetics production workshop produces and carries out homogenizing adjustment, improves the handlability of waste water, reduces issuablely in biochemical treatment process to go out load;
Described grating tank lattice are except the granular solids in cosmetic-producing wastewater and floating matter, and the front of grating tank vertically arranges coarse rack, cross except macrobead solid and floating matter; The tilting fine fack in back, filters slightly little granular solids and floating matter;
Described air flotation pool, comprise be connected with outside sewage water inlet pipe air flotation pool exposure chamber, release room, gas-floating chamber, dissolved air water storage chamber, mud room, the leveling board making sewage repeatedly be folded to flowing is provided with in described air flotation pool exposure chamber, air flotation pool exposure chamber be provided with vertical partition wall between release room, the bottom of described vertical partition wall is provided with the connected entrance that air flotation pool exposure chamber is connected with release room; The first sloping core is provided with between described release room and gas-floating chamber, described release room is communicated with gas-floating chamber top, described dissolved air water storage chamber is positioned at the below of mud room, centre is separated by dividing plate, be provided with flap between described gas-floating chamber and dissolved air water storage chamber, mud room, described flap is arranged with the connected entrance that gas-floating chamber is communicated with dissolved air water storage chamber; Described gas-floating chamber upper end is provided with slag scraper;
Described coagulative precipitation tank removes suspended solid thing in waste water and tensio-active agent and organism, and described coagulative precipitation tank is circumscribed with chemicals dosing plant;
Described anaerobic pond, to the biological degradation of pressure oxygen, is provided with the cleaning microporous aeration disc in pond and the sludge stirring machine for stirring double oxygen mud in anaerobic pond;
Small organic molecule in waste water is degraded to water, carbonic acid gas and inorganic salt by described Aerobic Pond, and the bottom even of Aerobic Pond is covered with as bacteria metabolism provides the microporous aeration disc of required dissolved oxygen.
2. the Waste Water Treatment of cosmetics production according to claim 1, is characterized in that: described coagulative precipitation tank and the external sludge thickener of anaerobic pond, and described sludge thickener connects pressure filter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520952404.0U CN205188076U (en) | 2015-11-26 | 2015-11-26 | Effluent disposal system of cosmetics production |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520952404.0U CN205188076U (en) | 2015-11-26 | 2015-11-26 | Effluent disposal system of cosmetics production |
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| CN205188076U true CN205188076U (en) | 2016-04-27 |
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| CN201520952404.0U Expired - Fee Related CN205188076U (en) | 2015-11-26 | 2015-11-26 | Effluent disposal system of cosmetics production |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106517646A (en) * | 2016-11-14 | 2017-03-22 | 深圳市贝优通新能源技术开发有限公司 | Wastewater treatment system for treating cosmetics wastewater |
| CN108558143A (en) * | 2018-05-24 | 2018-09-21 | 泾县吉祥纸业有限公司 | Sewage treatment equipment in a kind of processing of rice paper |
| CN108911218A (en) * | 2018-08-11 | 2018-11-30 | 段康伟 | A kind of aquaculture wastewater processing equipment |
| CN110054355A (en) * | 2019-04-19 | 2019-07-26 | 宁波斯蒂罗科技有限公司 | A kind of discharge treatment method of cosmetics cleaning waste water |
| CN112607960A (en) * | 2020-11-27 | 2021-04-06 | 山西焦化股份有限公司 | Optimization and improvement method for biochemical treatment load in wastewater treatment |
| CN113072247A (en) * | 2021-03-23 | 2021-07-06 | 昆山水清华环保科技有限公司 | Cosmetics sewage treatment system |
-
2015
- 2015-11-26 CN CN201520952404.0U patent/CN205188076U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106517646A (en) * | 2016-11-14 | 2017-03-22 | 深圳市贝优通新能源技术开发有限公司 | Wastewater treatment system for treating cosmetics wastewater |
| CN108558143A (en) * | 2018-05-24 | 2018-09-21 | 泾县吉祥纸业有限公司 | Sewage treatment equipment in a kind of processing of rice paper |
| CN108911218A (en) * | 2018-08-11 | 2018-11-30 | 段康伟 | A kind of aquaculture wastewater processing equipment |
| CN110054355A (en) * | 2019-04-19 | 2019-07-26 | 宁波斯蒂罗科技有限公司 | A kind of discharge treatment method of cosmetics cleaning waste water |
| CN112607960A (en) * | 2020-11-27 | 2021-04-06 | 山西焦化股份有限公司 | Optimization and improvement method for biochemical treatment load in wastewater treatment |
| CN113072247A (en) * | 2021-03-23 | 2021-07-06 | 昆山水清华环保科技有限公司 | Cosmetics sewage treatment system |
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Legal Events
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160427 Termination date: 20171126 |