CN106348492B - A kind of method that black printed Wastewater Pollutant extracts and prepares waste water decoloring agent - Google Patents
A kind of method that black printed Wastewater Pollutant extracts and prepares waste water decoloring agent Download PDFInfo
- Publication number
- CN106348492B CN106348492B CN201610904385.3A CN201610904385A CN106348492B CN 106348492 B CN106348492 B CN 106348492B CN 201610904385 A CN201610904385 A CN 201610904385A CN 106348492 B CN106348492 B CN 106348492B
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- Prior art keywords
- sludge
- waste water
- mud
- pollutant
- black printed
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/24—Treatment of water, waste water, or sewage by flotation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/14—Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/308—Dyes; Colorants; Fluorescent agents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/16—Regeneration of sorbents, filters
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Physical Water Treatments (AREA)
- Removal Of Specific Substances (AREA)
Abstract
The present invention discloses a kind of method that black printed Wastewater Pollutant extracts and prepares waste water decoloring agent, the following steps are included: adding acid into black plastic printing waste water, 5-30min is stirred, pollutant is agglomerated, using gas floatation process or the precipitation method by mud-water separation and by sludge condensation;Calcium miberal powder and pumice granules are added into the sludge of concentration with conditioning of mud specific gravity, sludge is heated to 50-95 DEG C of dehydration while stirring after mixing evenly, sludge is made to form bulk;Blocky sludge hot is squeezed and dries or spontaneously dries;Sludge isolation air is heated to 450-650 DEG C of heat preservation 1-4h;Sludge is cooled to 50 DEG C or less and is broken into graininess, is uniformly mixed after spraying wetting agent solution, is prepared into floating type decolorising agent;By mud granule by aeration stirring in cationic dyeing waste water is added to, after mud granule recycles 450-650 DEG C of hot recycling, it is recycled.The present invention realizes the extraction of black printed Wastewater Pollutant and the resource utilization of solid waste, and makes cationic dyeing decolorization rate of wastewater up to 99.5% or more.
Description
Technical field
The invention belongs to environmental engineering technical field, in particular to a kind of black printed Wastewater Pollutant extracts and system
The method of standby waste water decoloration of cation dyes agent.
Background technique
Water-based ink is because its environmental protection, security application range constantly expand, according to incompletely statistics, the use of Chinese water-based ink
Amount is just with 20% or more speed increase.A large amount of plastics package (waterproof) material uses aqueous oil in stamp more and more
Ink produces a certain amount of printing waste water in process of production.This kind of wastewater through organic matter content is high, the COD of usual waste waterCr:
5000-30000 mg/L;Coloration: 5000-20000 times.Wastewater biodegradability is poor, pollutes extremely serious, it is more difficult to handle.
Processing for this kind of waste water is usually first pre-processed using partition method, such as coagulating sedimentation or mixed condensed gas flotation process,
First dosing coagulant makes Organic Pollutants in Wastewater agglomerate to form sludge, then using the removal of the solid-liquid separating methods such as precipitating or air bearing
Suspension pollutant in waste water, water outlet carry out other chemistry or biological treatment again, realize rear discharge up to standard.What mud-water separation generated
Sludge carries out landfill disposal usually as solid waste by forming mud cake after mechanism filter-pressing or centrifugal dehydration, has both be easy to cause secondary dirt
Dye, and can not achieve resource utilization.
Summary of the invention
It is extracted the purpose of the present invention is to provide a kind of black water ink jet printing Wastewater Pollutant and preparation cation contaminates
Expect the method for waste water decoloring agent.
For achieving the above object, the technology of the present invention method uses following steps:
Acid is added into black plastic printing waste water, is stirred 5-30min, is agglomerated pollutant, using gas floatation process or precipitating
Method is by mud-water separation and by sludge condensation to solid content 5%-10%;The calcium miberal powder and 10- of 5-10g/L are added into the sludge of concentration
Sludge is heated to 50-95 DEG C of dehydration while stirring after mixing evenly, is made dirt by the pumice granules of 50g/L with conditioning of mud specific gravity
Mud forms bulk;Blocky sludge hot is squeezed and dries or spontaneously dries after being lower than 50% to moisture content;By sludge isolation air heating
To 450-650 DEG C of heat preservation 1-4h;Sludge is cooled to 50 DEG C or less and is broken into graininess, uniformly spraying mass concentration is 0.1-
It is uniformly mixed after 0.2% wetting agent solution, improves surface hydrophilicity, be prepared into floating type decolorising agent;Mud granule is pressed into 2-
10g/L waste water dosage is added in cationic dyeing waste water, and aeration stirring 10-180min can be such that decolorization rate of wastewater reaches
99.5% or more, it air bearing or filters to isolate mud granule and recycles;After recycling 450-650 DEG C of hot recycling of mud granule, circulation makes
With.
The utility model has the advantages that
A. black plastic printing waste water is treated by the present method, and percent of decolourization is up to 99.7% or more, CODCrRemoval rate reaches
90% or more, pollutant recovery rate realizes the resource utilization of solid waste up to 90% or more;
B. cationic dyeing waste water is added the floating type bleaching agent bleaching processing of preparation, and decolorization rate of wastewater reaches
99.5% or more and it is easy to mud-water separation.
Specific embodiment
The present invention is further illustrated below by specific embodiment.
Embodiment 1
Acid is added into black plastic printing waste water, 10min is stirred, agglomerates pollutant, is divided muddy water using gas floatation process
From and by sludge condensation to solid content 7.3%;The calcium miberal powder of 7.3g/L and the pumice granules of 30g/L are added into the sludge of concentration
With conditioning of mud specific gravity, sludge is heated to 85 DEG C of dehydrations while stirring after mixing evenly, sludge is made to form bulk;It will be blocky dirty
Mud hot pressing is squeezed to moisture content lower than 100 DEG C of drying after 50%;Sludge isolation air is heated to 500 DEG C of heat preservation 2h;Sludge is cooled down
It is broken into graininess to 50 DEG C or less, is uniformly mixed, improves after uniformly spraying the wetting agent solution that mass concentration is 0.1-0.2%
Surface hydrophilicity is prepared into floating type decolorising agent;Mud granule is added to the red dye of positive ion by 10g/L waste water dosage
In dyeing waste-water, aeration stirring 30min, up to 99.7% or more, filtering removal mud granule simultaneously recycles decolorization rate of wastewater;Recycling is dirty
After 500 DEG C of hot recyclings of mud particle, it is recycled in cationic dyeing waste water decoloring.
500 DEG C of hot recyclings, 10 mud granules are added continuously to cationic yellow dyes dyeing by 8g/L waste water dosage
In waste water, stirring 20min makes waste water decoloring, cationic yellow dyes dyeing waste-water decolorizing rate 99.6% after filtering.
Embodiment 2
Acid is added into black plastic printing waste water, 15min is stirred, agglomerates pollutant, is divided muddy water using gas floatation process
From and by sludge condensation to solid content 7.0%;The calcium miberal powder of 7.0g/L and the pumice granules of 25g/L are added into the sludge of concentration
With conditioning of mud specific gravity, sludge is heated to 80 DEG C of dehydrations while stirring after mixing evenly, sludge is made to form bulk;It will be blocky dirty
Mud hot pressing is squeezed to moisture content lower than 100 DEG C of drying after 50%;Sludge isolation air is heated to 550 DEG C of heat preservation 2h;Sludge is cooled down
It is broken into graininess to 50 DEG C or less, is uniformly mixed, improves after uniformly spraying the wetting agent solution that mass concentration is 0.1-0.2%
Surface hydrophilicity is prepared into floating type decolorising agent;Mud granule is added to mixed-cation dyestuff by 8g/L waste water dosage
In dyeing waste-water, aeration stirring 30min, up to 99.5% or more, filtering removal mud granule simultaneously recycles decolorization rate of wastewater;Recycling is dirty
After 500 DEG C of hot recyclings of mud particle, it is recycled in cationic dyeing waste water decoloring.
500 DEG C of hot recyclings, 10 mud granules are added continuously to blue cationic dyeing by 6g/L waste water dosage
In waste water, stirring 30min makes waste water decoloring, blue 99.8% or more cationic dyeing decolorization rate of wastewater after filtering.
Using the method for the present invention, the high efficiency extraction and resource utilization of pollutant in black plastic printing waste water are realized,
Secondary pollution is prevented, and cationic dyeing decolorization rate of wastewater is made to reach 99.5% or more, decolorization rate is fast, particle
Easily precipitating, opens the new way that solid wastes recycling utilizes.
Claims (2)
1. a kind of method that black printed Wastewater Pollutant extracts and prepares waste water decoloring agent, which is characterized in that including following step
It is rapid:
It adds acid into black printed waste water, stirs 5-30min, agglomerate pollutant, using gas floatation process or the precipitation method by muddy water
It separates and adjusts sludge to solid content 5%-10%;
The calcium miberal powder of 5-10g/L and the pumice granules of 10-50g/L are added into the sludge of concentration, after mixing evenly while stirring
Sludge is heated to 80-95 DEG C of dehydration, sludge is made to form bulk;
Blocky sludge hot is squeezed and dries or spontaneously dries after being lower than 50% to moisture content;
Sludge isolation air is heated to 450-650 DEG C of heat preservation 1-4h;
Sludge is cooled to 50 DEG C or less and is broken into graininess, uniformly sprays the wetting agent that a certain amount of mass concentration is 0.1-0.2%
It is uniformly mixed after solution, is prepared into floating type decolorising agent;
Mud granule is added in cationic dyeing waste water by 2-10g/L waste water dosage, aeration stirring 10-180min
Make waste water decoloring, air bearing or filters to isolate mud granule and recycle;450-650 DEG C of hot recycling of mud granule is recycled, circulation makes
With;
Wherein, the acid is inorganic acid or organic acid;The calcium miberal powder is or mixtures thereof calcium carbonate, calcium oxide;It is described
Wetting agent be or mixtures thereof non-ionic or anionic wetting agent.
2. the method that a kind of black printed Wastewater Pollutant according to claim 1 extracts and prepares waste water decoloring agent,
It is characterized in that the pumice granules are 100-400 mesh.
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CN201610904385.3A CN106348492B (en) | 2016-10-18 | 2016-10-18 | A kind of method that black printed Wastewater Pollutant extracts and prepares waste water decoloring agent |
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CN201610904385.3A CN106348492B (en) | 2016-10-18 | 2016-10-18 | A kind of method that black printed Wastewater Pollutant extracts and prepares waste water decoloring agent |
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CN106348492A CN106348492A (en) | 2017-01-25 |
CN106348492B true CN106348492B (en) | 2019-11-19 |
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CN108192660A (en) * | 2017-12-20 | 2018-06-22 | 中国石油大学(华东) | Dehydrating aging agent prescription and its dewatering process |
CN109126708A (en) * | 2018-09-20 | 2019-01-04 | 青岛大学 | A kind of adsorption decolouriser preparation method containing photochemical catalyst |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101362073A (en) * | 2008-09-27 | 2009-02-11 | 山东大学 | Preparation method of acidification sludge bentonite granules |
CN102205964A (en) * | 2011-04-25 | 2011-10-05 | 山东大学 | Granular activated carbon filler for paper mill sludge and preparation method thereof |
CN103752274A (en) * | 2013-12-12 | 2014-04-30 | 西北农林科技大学 | Amphiprotic-Gemini type cationic composite adsorbent, and preparation method thereof |
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Publication number | Priority date | Publication date | Assignee | Title |
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CN101811021B (en) * | 2010-04-26 | 2011-12-14 | 西北农林科技大学 | Amphiphilic adsorbent capable of adsorbing both organic matter and heavy metal cation and preparation method thereof |
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Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101362073A (en) * | 2008-09-27 | 2009-02-11 | 山东大学 | Preparation method of acidification sludge bentonite granules |
CN102205964A (en) * | 2011-04-25 | 2011-10-05 | 山东大学 | Granular activated carbon filler for paper mill sludge and preparation method thereof |
CN103752274A (en) * | 2013-12-12 | 2014-04-30 | 西北农林科技大学 | Amphiprotic-Gemini type cationic composite adsorbent, and preparation method thereof |
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Address after: 266071 No. 7 East Hongkong Road, Laoshan District, Shandong, Qingdao Patentee after: QINGDAO University Address before: 266071 Ningxia Road, Shandong, China, No. 308, No. Patentee before: QINGDAO University |
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