CN1830845A - Treatment technology of p-aminotoluene waste water - Google Patents
Treatment technology of p-aminotoluene waste water Download PDFInfo
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- CN1830845A CN1830845A CNA2006100389299A CN200610038929A CN1830845A CN 1830845 A CN1830845 A CN 1830845A CN A2006100389299 A CNA2006100389299 A CN A2006100389299A CN 200610038929 A CN200610038929 A CN 200610038929A CN 1830845 A CN1830845 A CN 1830845A
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- waste water
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- totuidine
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- iron charcoal
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
A process for treating the p-methylaniline sewage includes such steps as adding formaldehyde and aluminum sulfate, polycondensation reaction while generating polycondensate, adding high-molecular flocculant polyacrylamide, depositing, treating by Fe-C method, mixing the treated water with other industrial sewages, and areobic biochemical treating.
Description
Technical field:
The present invention relates to a kind of para-totuidine wastewater treatment method, belong to the chemical wastewater treatment technical field.
Technical background:
The production technique of para-totuidine is as follows
Contain benzene class and amino benzenes compounds in its factory effluent, according to the characteristics that aniline toxicity is big in the para-totuidine waste water, concentration is high, directly discharging does not reach national secondary discharge standard if do not carry out wastewater treatment, does not meet national requirements for environmental protection.
Summary of the invention:
The object of the present invention is to provide a kind of para-totuidine wastewater treatment method that can reach national secondary discharge standard.
The object of the present invention is achieved like this: a kind of para-totuidine wastewater treatment method, it is characterized in that: in para-totuidine waste water, add formaldehyde and Tai-Ace S 150 and carry out polycondensation and generate condenses separating out, add polymeric flocculant polyacrylamide precipitation then.Amino benzenes compounds content declines to a great extent in the waste water thereby make.Handle with iron charcoal method then, the water outlet of iron charcoal reaction tower and other trade effluent reach national secondary discharge standard after being mixed into the oxygen biochemical treatment of acting charitably.
Concrete processing step comprises:
Step 1, polycondensation
With sulphur acid for adjusting pH value to 5.5～6.5, the temperature of control waste water adds formaldehyde and Tai-Ace S 150 more than 80 ℃ in waste water, stir and make amino benzenes compounds and formaldehyde generation polycondensation, back flow reaction 30～120 minutes.Add polymkeric substance that Tai-Ace S 150 can solve generation and be attached on this difficult problem on the wall of reactor and the agitator.
Step 2, flocculation sediment
Add polymeric flocculant polyacrylamide precipitate and separate in the waste water after the polycondensation.
Step 3, iron charcoal method are handled
Supernatant liquor behind the flocculation sediment advances iron charcoal reaction tower with sulphur acid for adjusting pH value to 2～3.Filler is made up of iron plane flower and granulated active carbon in this tower.Wherein the iron plane flower is 4～6: 1 with the granulated active carbon weight ratio, and waste water stopped 4～12 hours in iron charcoal reaction tower,
Step 4, in and coagulating
The water outlet of iron charcoal reaction tower adds alkali lye and regulates pH=8.5～9, adds polymeric flocculant polyacrylamide (PAM) and promotes flocculation sediment, and toxicant and other organism further are removed.
Step 5, biochemical treatment
Above-mentioned waste water through the removal biochemical inhibitor mixes with other trade effluent, handles by aerobe, and organism is significantly degraded.Hydraulic detention time is 24～40.After the second pond mud-water separation, water outlet chemical oxygen demand (COD) (COD) satisfies national secondary discharge standard less than 150mg/L.
Description of drawings:
Fig. 1 is a process flow diagram of the present invention.
Embodiment:
The present invention is a kind of para-totuidine wastewater treatment method, it is in para-totuidine waste water, add formaldehyde and carry out polycondensation and generate condenses separating out, add polymeric flocculant polyacrylamide (PAM) precipitation then, amino benzenes compounds content declines to a great extent in the waste water thereby make.Handle with iron charcoal method then, the water outlet of iron charcoal reaction tower and other trade effluent reach national secondary discharge standard after being mixed into the oxygen biochemical treatment of acting charitably.Its concrete processing step is referring to Fig. 1:
Step 1, polycondensation
Para-totuidine waste water is collected to equalizing tank I.Xiang Chizhong adds sulfuric acid (concentration≤50%) and regulates pH value to 6, adopts pneumatic blending, makes to mix.Equalizing tank I waste water rises to enamel reaction still with pump, starts stirrer after adding formaldehyde and Tai-Ace S 150.Steam heating was 80-85 ℃ of following back flow reaction 120 minutes.The dosage of formaldehyde is pressed 1.5 times of mol ratios of aniline amount in the waste water.
For example, added amount of chemical is (weight ratio) during the aniline concentration 3000mg/L left and right sides:
38% formaldehyde 0.4%
Solid sulphuric acid aluminium 0.4%
The enamel reaction still water outlet flows into intermediate pool, naturally cooling, and then be transported to flocculation sedimentation tank.
Step 2, flocculation sediment
The intermediate pool water outlet to flocculation sedimentation tank, is stirred adding polymeric flocculant polyacrylamide (PAM) down with pump delivery.Dosage is 8 gram/ton waste water, visual practical situation adjustment.Stop to stir when great quantity of floc occurring.Natural subsidence, supernatant liquid is from flowing to equalizing tank II, and lower floor's mud is transported to sludge thickener with in-line pump.
Step 3, iron charcoal method
The supernatant liquid of flocculation sedimentation tank is pooled to equalizing tank II.In this pond, add sulfuric acid (concentration≤50%) and regulate pH to 2～3, adopt pneumatic blending in the pond, make to mix.Be transported to iron charcoal tower with acid proof pump.
Filler in the iron charcoal tower is made up of with granulated active carbon the iron plane flower: wherein the iron plane flower is 4～6: 1 with the granulated active carbon weight ratio, drops into successively in the tower, makes the two distribution even as far as possible.Waste water stopped 12 hours in iron charcoal tower.Add the iron plane flower to guarantee its normal operation according to waste.
Step 4, in and coagulating
The neutralization reaction pond is divided into three lattice, and waste water flows through successively.First lattice add lime, by pH on-line monitoring instrument control pH=8.5～9, adopt mechanical stirring.Second lattice are reaction zone, adopt pneumatic blending.The 3rd lattice add polymeric flocculant polyacrylamide (PAM), adopt pneumatic blending to make and mix.
Waste water advances the tube settler solid-liquid separation.The mud of tube settler bottom arrives sludge treating system with pump delivery.Decide on practical situation several times weekly.
Step 5, biochemical treatment
The tube settler supernatant liquor flows into equalizing tank III, mixes with other trade effluents.Establish pneumatic blending in the pond, make to mix.And then equalizing tank III waste water risen to biochemical system with pump.
Semi soft packing is installed in the aerobic biochemical pond, and the filler filling ratio is 62.3%.Aerating system 1 cover (KBB micro-hole aerator, UPVC pipe), intermittent aeration, control dissolved oxygen content (DO) is at 2～4mg/L.Retention time of sewage 40 hours.
The Aerobic Pond bio-chemical effluent is through the second pond precipitate and separate, and water outlet chemical oxygen demand (COD) (COD) satisfies national secondary discharge standard less than 150mg/L.
Second pond mud enters sedimentation once more behind the sludge thickener, and to plate-and-frame filter press, the concentration basin supernatant liquor is delivered to the intermediate pool circular treatment to excess sludge by pump delivery.
Claims (4)
1, a kind of para-totuidine wastewater treatment method, it is characterized in that: in para-totuidine waste water, adding formaldehyde and Tai-Ace S 150 carries out polycondensation and generates condenses separating out, add polymeric flocculant polyacrylamide precipitation then, handle with iron charcoal method then, the water outlet of iron charcoal reaction tower mixes the laggard oxygen biochemical treatment of acting charitably with other trade effluent.
2, a kind of para-totuidine wastewater treatment method according to claim 1, it is characterized in that: its concrete processing step comprises:
Step 1, polycondensation
With sulphur acid for adjusting pH value to 5.5～6.5, the temperature of control waste water adds formaldehyde and Tai-Ace S 150 more than 80 ℃ in waste water, and stir and make amino benzenes compounds and formaldehyde generation polycondensation, back flow reaction 30～120 minutes,
Step 2, flocculation sediment
Add polymeric flocculant polyacrylamide precipitate and separate in the waste water after the polycondensation,
Step 3, iron charcoal method are handled
Supernatant liquor behind the flocculation sediment advances iron charcoal reaction tower with sulphur acid for adjusting pH value to 2～3, and filler is made up of iron plane flower and granulated active carbon in this tower, and wherein the iron plane flower is 4～6: 1 with the granulated active carbon weight ratio, and waste water stopped 4～12 hours in iron charcoal reaction tower,
Step 4, in and coagulating
The water outlet of iron charcoal reaction tower adds alkali lye and regulates pH=8.5～9, and add the polymeric flocculant polyacrylamide and promote flocculation sediment,
Step 5, biochemical treatment
Above-mentioned waste water through the removal biochemical inhibitor mixes with other trade effluent, handles by aerobe, and organism is significantly degraded, and hydraulic detention time is 24～40 hours, after the second pond mud-water separation, and water outlet.
3, a kind of para-totuidine wastewater treatment method according to claim 2, it is characterized in that: its concrete processing step comprises:
Step 1, polycondensation
Para-totuidine waste water is collected to equalizing tank I, Xiang Chizhong adds sulphur acid for adjusting pH value to 6, sulfuric acid concentration≤50%, adopt pneumatic blending, make to mix, equalizing tank I waste water rises to enamel reaction still with pump, start stirrer after adding formaldehyde and Tai-Ace S 150, steam heating was 80-85 ℃ of following back flow reaction 120 minutes, and the dosage of formaldehyde is pressed 1.5 times of mol ratios of aniline amount in the waste water
The reactor water outlet flows into intermediate pool, naturally cooling, and then be transported to flocculation sedimentation tank,
Step 2, flocculation sediment
The intermediate pool water outlet to flocculation sedimentation tank, is stirred adding polymeric flocculant polyacrylamide down with pump delivery, and dosage is 8 gram/ton waste water, stop to stir when great quantity of floc occurring, natural subsidence, supernatant liquid is from flowing to equalizing tank II, lower floor's mud is transported to sludge thickener with in-line pump
Step 3, iron charcoal method are handled
The supernatant liquid of flocculation sedimentation tank is pooled to equalizing tank II, adds sulfuric acid and regulate pH to 2～3 in this pond, and sulfuric acid concentration≤50% adopts pneumatic blending in the pond, make to mix, and is transported to iron charcoal tower with acid proof pump, and waste water stopped 12 hours in iron charcoal tower,
Step 4, in and coagulating
The neutralization reaction pond is divided into three lattice, and waste water flows through successively, and first lattice add lime, by pH on-line monitoring instrument control pH=8.5～9, adopt mechanical stirring, second lattice are reaction zone, adopt pneumatic blending, the 3rd lattice add the polymeric flocculant polyacrylamide, adopt pneumatic blending to make and mix
Waste water advances the tube settler solid-liquid separation, and the mud of tube settler bottom arrives sludge treating system with pump delivery,
Step 5, biochemical treatment
The tube settler supernatant liquor flows into equalizing tank III, mixes with other trade effluents, establishes pneumatic blending in the pond, and make to mix, and then equalizing tank III waste water is risen to biochemical system with pump,
Semi soft packing is installed in the aerobic biochemical pond, the filler filling ratio is 62.3%, aerating system one cover, intermittent aeration, control dissolved oxygen content 2～4mg/L, retention time of sewage 40 hours, the Aerobic Pond bio-chemical effluent is through the second pond precipitate and separate, water outlet, and second pond mud enters sedimentation once more behind the sludge thickener, to plate-and-frame filter press, the concentration basin supernatant liquor is delivered to the intermediate pool circular treatment to excess sludge by pump delivery.
4, according to claim 1 or 2,3 described a kind of para-totuidine wastewater treatment method, it is characterized in that: described polymeric flocculant polyacrylamide is configured to 0.08～0.12% solution.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100389299A CN100391874C (en) | 2006-03-17 | 2006-03-17 | Treatment technology of p-aminotoluene waste water |
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| Application Number | Priority Date | Filing Date | Title |
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| CNB2006100389299A CN100391874C (en) | 2006-03-17 | 2006-03-17 | Treatment technology of p-aminotoluene waste water |
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| CN1830845A true CN1830845A (en) | 2006-09-13 |
| CN100391874C CN100391874C (en) | 2008-06-04 |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103466885A (en) * | 2013-09-12 | 2013-12-25 | 安徽省绿巨人环境技术有限公司 | Process for treating wastewater generated in solar silicon wafer production process |
| CN104445711A (en) * | 2014-10-29 | 2015-03-25 | 绍兴奇彩化工有限公司 | Treatment method for aniline wastewater |
| CN106630421A (en) * | 2016-12-21 | 2017-05-10 | 中国石油天然气集团公司 | Phenylamine wastewater treatment method and device |
| CN108975628A (en) * | 2018-08-20 | 2018-12-11 | 朱翠帮 | A kind for the treatment of process of mining area sewage |
| CN113104946A (en) * | 2021-04-01 | 2021-07-13 | 时代沃顿科技有限公司 | Method for treating wastewater containing polyamino aromatic compounds |
| CN114426363A (en) * | 2022-01-29 | 2022-05-03 | 深圳市中科纳米科技有限公司 | Degradation treatment method for treating liquid waste organic matters |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6627086B2 (en) * | 2001-03-21 | 2003-09-30 | Polymer Ventures, Inc. | Methods of producing polyarylamines and using them for detackifying paint and removing color from aqueous systems |
| CN100417604C (en) * | 2004-12-22 | 2008-09-10 | 中国石化集团南京化学工业有限公司 | Fully biological treatment of wastewater of nitrobenzol or aniline or their mixture |
-
2006
- 2006-03-17 CN CNB2006100389299A patent/CN100391874C/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103466885A (en) * | 2013-09-12 | 2013-12-25 | 安徽省绿巨人环境技术有限公司 | Process for treating wastewater generated in solar silicon wafer production process |
| CN104445711A (en) * | 2014-10-29 | 2015-03-25 | 绍兴奇彩化工有限公司 | Treatment method for aniline wastewater |
| CN106630421A (en) * | 2016-12-21 | 2017-05-10 | 中国石油天然气集团公司 | Phenylamine wastewater treatment method and device |
| CN108975628A (en) * | 2018-08-20 | 2018-12-11 | 朱翠帮 | A kind for the treatment of process of mining area sewage |
| CN113104946A (en) * | 2021-04-01 | 2021-07-13 | 时代沃顿科技有限公司 | Method for treating wastewater containing polyamino aromatic compounds |
| CN114426363A (en) * | 2022-01-29 | 2022-05-03 | 深圳市中科纳米科技有限公司 | Degradation treatment method for treating liquid waste organic matters |
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| CN100391874C (en) | 2008-06-04 |
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