CN204325020U - A kind of device of full automatic treatment pigment dyestuff industry waste water - Google Patents
A kind of device of full automatic treatment pigment dyestuff industry waste water Download PDFInfo
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- CN204325020U CN204325020U CN201420516969.XU CN201420516969U CN204325020U CN 204325020 U CN204325020 U CN 204325020U CN 201420516969 U CN201420516969 U CN 201420516969U CN 204325020 U CN204325020 U CN 204325020U
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- Prior art keywords
- tank
- storage tank
- water
- wastewater storage
- waste water
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- Expired - Fee Related
Links
- 239000002351 wastewater Substances 0.000 title claims abstract description 65
- 239000000049 pigment Substances 0.000 title claims abstract description 17
- 239000000975 dye Substances 0.000 title claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 61
- 239000003814 drug Substances 0.000 claims abstract description 32
- 238000010521 absorption reaction Methods 0.000 claims abstract description 27
- 239000011347 resin Substances 0.000 claims abstract description 21
- 229920005989 resin Polymers 0.000 claims abstract description 21
- 239000003513 alkali Substances 0.000 claims description 6
- 239000003795 chemical substances by application Substances 0.000 claims description 6
- 239000010802 sludge Substances 0.000 claims description 3
- 239000002562 thickening agent Substances 0.000 claims description 3
- 239000012860 organic pigment Substances 0.000 abstract description 16
- 238000000034 method Methods 0.000 abstract description 13
- 230000008569 process Effects 0.000 abstract description 11
- 238000005516 engineering process Methods 0.000 abstract description 5
- 238000006243 chemical reaction Methods 0.000 abstract description 4
- 238000001179 sorption measurement Methods 0.000 abstract description 4
- 239000007789 gas Substances 0.000 description 7
- 239000000243 solution Substances 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
- 238000004065 wastewater treatment Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 2
- 239000010815 organic waste Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 239000000976 ink Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- IEQIEDJGQAUEQZ-UHFFFAOYSA-N phthalocyanine Chemical compound N1C(N=C2C3=CC=CC=C3C(N=C3C4=CC=CC=C4C(=N4)N3)=N2)=C(C=CC=C2)C2=C1N=C1C2=CC=CC=C2C4=N1 IEQIEDJGQAUEQZ-UHFFFAOYSA-N 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Landscapes
- Water Treatment By Sorption (AREA)
Abstract
The utility model relates to a kind of device of full automatic treatment pigment dyestuff industry waste water, comprise: wastewater storage tank, resin absorption tank, clean water tank, PLC control system and medicine system, it is characterized in that, be provided with a pH value in described wastewater storage tank and detect meter, survey TOC instrument and an agitator online; Described clean water tank is provided with one and surveys TOC instrument online; Described medicine system is connected with resin absorption tank and wastewater storage tank pipeline, the water outlet of this wastewater storage tank is connected with the water-in pipeline of this absorption storage tank by impeller pump, this absorption water outlet is connected with the water-in pipeline of this clean water tank, and this clean water tank is connected with extraneous and wastewater storage tank pipeline.Advantage of the present utility model: structure is simple, easy to use, by the combination of chemical reaction and adsorption technology, and utilizes PLC to carry out Automatic Control, can process organic pigment waste water quick, efficient, energy-conservationly.Meanwhile, the time is short, it is little to take up an area, it is fast to run, reduce artificially participate in, water outlet is better than integrated wastewater discharge standard " GB8978-1996 " I grade standard, overcome simultaneously existing can not the shortcoming of automatization.
Description
Technical field
The utility model relates to organic pigment waste water processing technology field, particularly a kind of device of full automatic treatment pigment dyestuff industry waste water.
Background technology
Pigment dyestuff refers to a class pigment that have color and other a series of pigment characteristics, that be made up of organic compound.Pigment dyestuff is widely used in the industries such as coating, ink and plastics, can discharge organic waste water, dust and waste gas in process of production, wherein organic waste water to the pollution of water surrounding more greatly.
The factory effluent of pigment dyestuff has high COD
cr, high chroma, supersalinity, organism bio-refractory, add the discharge of waste water intermittence, water quality and quantity change greatly in time, be difficult to adopt conventional treatment process to administer.
Chinese patent (CN100482603C) authorizes a kind of deep treatment method of organic pigment waste water, its key step comprises: first pigment wastewater is carried out electrolysis, enter anaerobic grain bed bioreactor after wastewater dilution, then after entering aerobic reactor process, water outlet reaches national grade one discharge standard.But this kind of method cultivation time is long, long reaction time, therefore, floor space is large, and the effect of microbiological treatment is unstable, can not full automatic control.
Utility model content
The utility model object overcomes prior art systems complex structure, the deficiency that can not automatically manage, there is provided a kind for the treatment of unit simple, comprise all treating processess and all automatically carry out, and automatically can record the treatment unit of full-automatic organic pigment waste water of wastewater treatment whole process.
To achieve these goals, the technical solution of the utility model is achieved in that a kind of device of full automatic treatment organic pigment waste water, comprise: wastewater storage tank, resin absorption tank, clean water tank, PLC control system and medicine system, it is characterized in that, be provided with a pH value in described wastewater storage tank and detect meter, survey TOC instrument and an agitator online; Described clean water tank is provided with one and surveys TOC instrument online; Described medicine system is connected with resin absorption tank and wastewater storage tank pipeline, the water outlet of this wastewater storage tank is connected with the water-in pipeline of this absorption storage tank by impeller pump, this absorption water outlet is connected with the water-in pipeline of this clean water tank, and this clean water tank is connected with extraneous and wastewater storage tank pipeline.
Preferentially, described medicine system comprises sour medicine system, alkali medicament system, discoloring agent medicine system, PAC medicine system and PAM medicine system, desorbed solution medicine system.Preferentially, adsorb between storage tank and clean water tank and be provided with water flow meter.
Preferentially, feed water flow gauge is provided with between described impeller pump and resin absorption tank.
Preferentially, described wastewater storage tank is connected with a sludge thickener pipeline.
Preferentially, the source of the gas of described aerating system is provided by the gas blower be arranged on outside wastewater storage tank.Preferentially, described resin is WR type, HP type, D type or H type.
Compared with prior art, structure is simple, and easy to use, the utility model make use of chemical reaction and adsorption technology effectively combines, and utilizes PLC to carry out Automatic Control, can process organic pigment waste water quick, efficient, energy-conservationly.Meanwhile, the time is short, it is little to take up an area, it is fast to run, reduce artificially participate in, water outlet is better than integrated wastewater discharge standard " GB8978-1996 " I grade standard, overcome simultaneously existing can not the shortcoming of automatization.
Accompanying drawing explanation
Fig. 1 is a kind of structural representation of the present utility model.
Wherein, 1-wastewater storage tank, 2-pH counts, 3-surveys TOC meter online, 4-impeller pump, 5-under meter, 6-resin adsorption tanks, 7-under meter, 8-clean water tank, 9-surveys TOC instrument online, 10-acid medicine system, 11-alkali medicine system, 12-discoloring agent medicine system, 13-PAC medicine system, 14-PAM medicine system, 15-desorbed solution medicine system, 16-gas blower.
Embodiment
Below in conjunction with drawings and Examples, the utility model is elaborated.
Shown in Fig. 1 is a kind of device of full automatic treatment organic pigment waste water, comprise: wastewater storage tank, resin absorption tank, clean water tank, PLC control system and medicine system, it is characterized in that, be provided with a pH value in described wastewater storage tank and detect meter (for detecting the pH value of waste water tank, auxiliary PLC is to the control of waste water potential of hydrogen), one surveys TOC instrument (the TOC concentration of wastewater measurement tank online, auxiliary PLC controls the amount of dosing automatically) and an aerating system (source of the gas is provided by the gas blower be arranged on outside wastewater storage tank), its opening for feed respectively with sour medicine system, alkali medicine system, PAC system, discoloring agent system is connected with PAM system pipeline, resin absorption tank is also connected with desorbed solution medicine system pipeline simultaneously, described clean water tank is provided with an on-line determination TOC instrument, for testing the TOC concentration of clean water tank, the water outlet of this wastewater storage tank is connected with the water-in pipeline of this resin absorption tank by impeller pump, the outlet of this resin absorption tank is connected with the water-in pipeline of this wastewater storage tank, also be connected with the water-in pipeline of this clean water tank, the water outlet of this clean water tank is connected with extraneous and wastewater storage tank pipeline respectively.Described clean water tank is also connected with absorption pipeline by described impeller pump.
Be provided with water flow meter between described resin absorption tank and clean water tank, between described impeller pump and resin absorption tank, be provided with feed water flow gauge.Feed water flow gauge, water flow meter are used for the situation of each pipeline flow rate of water flow of real time record, and whether prompting absorption normally runs.
Described wastewater storage tank is also connected with sludge thickener.
Organic pigment waste water enters wastewater storage tank, detects the numerical value measuring and arrive, add acid (alkali) by PLC control system calculation control acid (alkali) medicine system according to pH value, makes the pH value of wastewater storage tank be adjusted to alkalescence.According to the online detected result surveying TOC instrument, add flocculation agent by PLC control system control PAC, discoloring agent, PAM medicine system, generate precipitation.Be provided with aerating system in waste water storage tank, provide source of the gas by gas blower, for uniform stirring.After dosing terminates, aerating system stops automatically.After chemical reaction terminates, bottom 15% mud liquid is extracted out; 85% supernatant liquor enters resin absorption tank through impeller pump, and the bottom water outlet of resin absorption tank enters clean water basin, and clean water basin arrange one and survey TOC instrument online, if water quality reaching standard, are then discharged in the middle of river; If not up to standard, be then back in wastewater storage tank, carry out secondary treatment.
After being disposed, when need clear up resin absorption tank, enter resin absorption tank by PLC control desorbed solution and resolve, the water after parsing is back to wastewater storage tank.
Utilize said apparatus, obtain following test-results:
Embodiment 1
Process TOC(total organic carbon) concentration is the acid organic pigment waste water of 520mg/L, after organic pigment waste water treatment unit, TOC of yielding water is 22mg/L, COD is 71mg/L, pH7.3, water white transparency.
Embodiment 2
Process TOC is the azo organic pigment waste water of 387mg/L, and after organic pigment waste water treatment unit, TOC of yielding water is 12mg/L, COD is 57mg/L, pH8.2, water white transparency.
Embodiment 3
Process TOC is the phthalocyanine organic pigment waste water of 1237mg/L, and after organic pigment waste water treatment unit, TOC of yielding water is 18mg/L, COD is 62mg/L, pH7.5, water white transparency.
In above-mentioned example, result shows: the TOC content clearance in organic pigment waste water is 95-99%, and TOC of yielding water is stabilized in below 30mg/L, good decolorizing effect, and water outlet is as clear as crystal.Can obviously find out, device is removed TOC and is reached 95-99%, and level of automation is high, and water outlet meets sewage drainage standard " GB8978-1996 " I grade of emission standard, reaches designing treatment requirement.
Below only describe embodiment of the present utility model, it describes comparatively concrete and detailed, but therefore can not be interpreted as the restriction to utility model patent scope.It should be pointed out that for the person of ordinary skill of the art, without departing from the concept of the premise utility, can also make some distortion and improvement, these all belong to protection domain of the present utility model.Therefore, the protection domain of the utility model patent is as the criterion with claims.
Advantage of the present utility model: structure is simple, easy to use, by the combination of chemical reaction and adsorption technology, and utilizes PLC to carry out Automatic Control, can process organic pigment waste water quick, efficient, energy-conservationly.Meanwhile, the time is short, it is little to take up an area, it is fast to run, reduce artificially participate in, water outlet is better than integrated wastewater discharge standard " GB8978-1996 " I grade standard, overcome simultaneously existing can not the shortcoming of automatization.
Claims (7)
1. the device of a full automatic treatment pigment dyestuff industry waste water, comprise: wastewater storage tank, resin absorption tank, clean water tank, PLC control system and medicine system, it is characterized in that, be provided with a pH value in described wastewater storage tank and detect meter, survey TOC instrument and an agitator online; Described clean water tank is provided with one and surveys TOC instrument online; Described medicine system is connected with resin absorption tank and wastewater storage tank pipeline, the water outlet of this wastewater storage tank is connected with the water-in pipeline of this absorption storage tank by impeller pump, this absorption water outlet is connected with the water-in pipeline of this clean water tank, and this clean water tank is connected with extraneous and wastewater storage tank pipeline.
2. the device of a kind of full automatic treatment pigment dyestuff industry waste water according to claim 1, is characterized in that: described medicine system comprises sour medicine system, alkali medicament system, discoloring agent medicine system, PAC medicine system and PAM medicine system, desorbed solution medicine system.
3. the device of a kind of full automatic treatment pigment dyestuff industry waste water according to claim 1, is characterized in that: be provided with water flow meter between described absorption storage tank and clean water tank.
4. the device of a kind of full automatic treatment pigment dyestuff industry waste water according to claim 1, is characterized in that: be provided with feed water flow gauge between described impeller pump and resin absorption tank.
5. the device of a kind of full automatic treatment pigment dyestuff industry waste water according to claim 1, is characterized in that: described wastewater storage tank is connected with a sludge thickener pipeline.
6. the device of a kind of full automatic treatment pigment dyestuff industry waste water according to claim 1, is characterized in that: the source of the gas of described aerating system is provided by the gas blower be arranged on outside wastewater storage tank.
7. the device of a kind of full automatic treatment pigment dyestuff industry waste water according to claim 1, is characterized in that: described resin is WR type, HP type, D type or H type.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420516969.XU CN204325020U (en) | 2014-09-10 | 2014-09-10 | A kind of device of full automatic treatment pigment dyestuff industry waste water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420516969.XU CN204325020U (en) | 2014-09-10 | 2014-09-10 | A kind of device of full automatic treatment pigment dyestuff industry waste water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204325020U true CN204325020U (en) | 2015-05-13 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420516969.XU Expired - Fee Related CN204325020U (en) | 2014-09-10 | 2014-09-10 | A kind of device of full automatic treatment pigment dyestuff industry waste water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204325020U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107555668A (en) * | 2017-10-26 | 2018-01-09 | 佛山市宝粤美科技有限公司 | A kind of waste water full automatic purifier |
-
2014
- 2014-09-10 CN CN201420516969.XU patent/CN204325020U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107555668A (en) * | 2017-10-26 | 2018-01-09 | 佛山市宝粤美科技有限公司 | A kind of waste water full automatic purifier |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150513 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |