CN101708886B - Method for treating organic waste water - Google Patents
Method for treating organic waste water Download PDFInfo
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- CN101708886B CN101708886B CN200910234358XA CN200910234358A CN101708886B CN 101708886 B CN101708886 B CN 101708886B CN 200910234358X A CN200910234358X A CN 200910234358XA CN 200910234358 A CN200910234358 A CN 200910234358A CN 101708886 B CN101708886 B CN 101708886B
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- waste water
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 27
- 238000000034 method Methods 0.000 title claims abstract description 19
- 239000010815 organic waste Substances 0.000 title claims abstract description 18
- 239000000843 powder Substances 0.000 claims abstract description 20
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 claims abstract description 17
- 239000002245 particle Substances 0.000 claims abstract description 9
- 239000002244 precipitate Substances 0.000 claims abstract description 8
- 229960005070 ascorbic acid Drugs 0.000 claims abstract description 7
- 235000010323 ascorbic acid Nutrition 0.000 claims abstract description 7
- 239000011668 ascorbic acid Substances 0.000 claims abstract description 7
- 239000008367 deionised water Substances 0.000 claims abstract description 7
- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 12
- 230000008569 process Effects 0.000 claims description 8
- 229910052739 hydrogen Inorganic materials 0.000 claims description 6
- 229910052757 nitrogen Inorganic materials 0.000 claims description 6
- 230000010355 oscillation Effects 0.000 claims description 6
- 230000001105 regulatory effect Effects 0.000 claims description 6
- 239000012467 final product Substances 0.000 claims description 2
- 239000002957 persistent organic pollutant Substances 0.000 abstract description 6
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 abstract description 5
- 239000000463 material Substances 0.000 abstract description 4
- 230000009467 reduction Effects 0.000 abstract description 3
- 239000011435 rock Substances 0.000 abstract description 3
- 238000000926 separation method Methods 0.000 abstract description 2
- 238000001035 drying Methods 0.000 abstract 1
- 239000012299 nitrogen atmosphere Substances 0.000 abstract 1
- 238000001556 precipitation Methods 0.000 abstract 1
- 238000005406 washing Methods 0.000 abstract 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 11
- 238000006243 chemical reaction Methods 0.000 description 6
- 229910052742 iron Inorganic materials 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 4
- 229910052782 aluminium Inorganic materials 0.000 description 4
- 230000015556 catabolic process Effects 0.000 description 4
- 238000006731 degradation reaction Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000002594 sorbent Substances 0.000 description 4
- 239000002351 wastewater Substances 0.000 description 4
- CQPFMGBJSMSXLP-UHFFFAOYSA-M acid orange 7 Chemical compound [Na+].OC1=CC=C2C=CC=CC2=C1N=NC1=CC=C(S([O-])(=O)=O)C=C1 CQPFMGBJSMSXLP-UHFFFAOYSA-M 0.000 description 3
- 239000004411 aluminium Substances 0.000 description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 3
- 238000005119 centrifugation Methods 0.000 description 3
- 238000005868 electrolysis reaction Methods 0.000 description 3
- 229910052500 inorganic mineral Chemical class 0.000 description 3
- -1 iron ion Chemical class 0.000 description 3
- CXKWCBBOMKCUKX-UHFFFAOYSA-M methylene blue Chemical compound [Cl-].C1=CC(N(C)C)=CC2=[S+]C3=CC(N(C)C)=CC=C3N=C21 CXKWCBBOMKCUKX-UHFFFAOYSA-M 0.000 description 3
- 229960000907 methylthioninium chloride Drugs 0.000 description 3
- 239000011707 mineral Chemical class 0.000 description 3
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- 239000000701 coagulant Substances 0.000 description 2
- 238000005345 coagulation Methods 0.000 description 2
- 230000015271 coagulation Effects 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 2
- 230000002829 reductive effect Effects 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 239000004408 titanium dioxide Substances 0.000 description 2
- 239000003643 water by type Substances 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N Alumina Chemical compound [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical class O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 239000012028 Fenton's reagent Substances 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000031018 biological processes and functions Effects 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 235000011089 carbon dioxide Nutrition 0.000 description 1
- JYYOBHFYCIDXHH-UHFFFAOYSA-N carbonic acid;hydrate Chemical class O.OC(O)=O JYYOBHFYCIDXHH-UHFFFAOYSA-N 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229910001448 ferrous ion Inorganic materials 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000002638 heterogeneous catalyst Substances 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000010525 oxidative degradation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- NDLPOXTZKUMGOV-UHFFFAOYSA-N oxo(oxoferriooxy)iron hydrate Chemical compound O.O=[Fe]O[Fe]=O NDLPOXTZKUMGOV-UHFFFAOYSA-N 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 150000003254 radicals Chemical class 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000001603 reducing effect Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 229960001866 silicon dioxide Drugs 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 230000003245 working effect Effects 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Landscapes
- Water Treatment By Sorption (AREA)
Abstract
The invention discloses a method for treating organic waste water, which comprises: firstly, crushing volcanic rock and grinding the crushed volcanic rock into 10 to 60 mesh powder; adding 0.5 to 2 grams of the power into 20 milliliters of ascorbic acid solution at a concentration of 30 to 100mg/L, shaking the solution for 15 to 20 minutes, performing precipitation and separation, washing the precipitate with deionized water and drying the precipitate under the protection of a nitrogen atmosphere; adding the obtained powder particles into 50 milliliters of organic waste water, adjusting the pH value of the organic waste water to 1 to 6, and shaking the organic waste water for 30 minutes; and finally, adding 0.1 to 4 milliliters of 30 percent H2O2 and shaking with ultrasonic waves for 30 minutes to 1 hour to allow the organic matters in the water to degrade completely. The method has the advantages of simple operation, small material consumption, cheap and readily available material, high-efficiency removal of organic pollutants, equipment investment conservation and floor area occupation reduction.
Description
Technical field
The present invention relates to a kind of treatment process of organic waste water, belong to technical field of sewage in the environment protection.
Background technology
The quantity discharged of various organic waste waters increases year by year, brings huge challenge to water environment protection.The combination of treatment process general using biological process, physics method and chemical method and two or more methods of conventional organic waste water, but biological treatment such as activated sludge process also face the recovery and the ultimate disposal problem of active sludge simultaneously because of organic pollutant causes treatment of organic matters of organic inefficiency in the waste water to the toxic action of microorganism.Physics method such as absorption method make organic molecule be adsorbed on its surface or allow the filter bed of organic waste water by being made of sorbent particles, thereby reach the purpose of purification of organic waste water, yet sorbent material cost height, non-renewable, loading capacity is limited, general by modification to sorbent material, mention the absorption property and the work-ing life of sorbent material.Chemical method such as Coagulation Method, oxidation style, the coagulation rule need add a large amount of coagulating agent, the many and dehydration difficulty of body refuse amount, present research direction is the coagulating agent of development of new.Traditional homogeneous phase Fenton method is that ferrous ion and hydrogen peroxide react the extremely strong HO free radical of generation oxidisability under acidic conditions, HO has higher electronegativity and stronger electron affinity, can capture the H atom in the organic pollutant molecule, fill unsaturated carbon-to-carbon double bond or triple bond, show as strong oxidizing property, thereby oxidative degradation organic pollutant, even be harmless inorganicss such as carbonic acid gas, water and mineral salt with the organic pollutant oxygenolysis up hill and dale, can not produce new pollution, there is the problem of reaction back separation difficulty in the Fenton reaction.Therefore, most of at present research is devoted to develop the heterogeneous Fenton catalyzer of synthesizing efficient practicality.
The mineral rock that the magma condensation that sprays when volcanics is volcanic eruption forms, majority is made up of magmatite, and quality is loose, porous.Volcanics wherein contains elements such as abundant mineral calcium, magnesium, iron, zinc, aluminium mainly based on basalt in the world.Basaltic by analysis main component is: silicon-dioxide 45.2%, titanium dioxide 2.31%, aluminium sesquioxide 14.02%, ferric oxide 5.59%, iron protoxide 6.67% etc.Wherein contained iron, aluminium and part titanyl compound can be reduced into the simple substance fine particle under the effect of reductive agent xitix, these elemental metals are because reduction potential difference own can form galvanic cell, degradation of organic substances effectively, form iron ion or aluminum ion, in addition, titanium dioxide itself just has the effect of catalyzed degradation.After the little electrolysis of galvanic cell, add H again
2O
2, make full use of the Fe that is dissolved in the solution
2+, form the Fenton reaction, further decomposing organic matter utilizes ultrasonic wave to quicken organic matter degradation at last.This process is utilized natural heterogeneous catalyst volcanics, makes that the water treatment raw material is cheap and easy to get, the result economical and efficient, can be widely used in treatment of Organic Wastewater.
Summary of the invention
The treatment process that the purpose of this invention is to provide a kind of organic waste water has been utilized the contained special composition of volcanics, and cost is low and treatment effect good.
The technical solution used in the present invention is in turn include the following steps: earlier 10～60 purpose powder are pulverized and be milled into to volcanics; Get this powder 0.5～2g and join in the ascorbic acid solution that 20mL concentration is 30～100mg/L, vibration 15～20min, precipitate and separate, deionized water rinsing, nitrogen protection oven dry down; The powder particle that obtains is joined in the 50mL organic waste water, regulating pH is 1～6 again, vibration 30min; Add 0.1～4mL concentration at last and be 30% H
2O
2, auxiliary with ultra-sonic oscillation 30min～1h, organism is fully degraded get final product.
The invention has the beneficial effects as follows: (1) utilizes oxide compounds such as the activation iron that volcanics itself contained, aluminium, titanium, utilize the reducing property of xitix to become simple substance attached to the volcanics surface its partial reduction, form the little electrolysis of galvanic cell between the particle, simple to operate, consumptive material is few, and material is cheap and easy to get.(2) utilize the equal Fenton reagent of iron ion conduct that generates after little electrolysis, under acidic conditions, constitute the Fenton reaction, reach the purpose of efficient removal organic pollutant with hydrogen peroxide.(2) utilize the accelerated reaction of hyperacoustic " cavitation " effect to carry out, reaction is quickened, degradation of organic substances is saved facility investment and floor space rapidly.
Embodiment
10～60 purpose powder are pulverized and be milled into to volcanics; Get this powder 0.5～2g and join in the ascorbic acid solution that 20mL concentration is 30～100mg/L, vibration 15～20min, precipitate and separate, deionized water rinsing, nitrogen protection oven dry down; The powder particle that obtains is joined in the 50mL organic waste water, and regulating pH is 1～6, vibration 30min; Add 0.1～4mL concentration again and be 30% H
2O
2, auxiliary with ultra-sonic oscillation 30min～1h, organism is fully degraded.The xitix that the present invention uses is a kind of general organic reagent, can direct commercial acquisition, have reductibility.
The present invention is further illustrated below by the embodiment of 3 concrete organic waste waters:
Embodiment 1
10 purpose powder are pulverized and be milled into to volcanics; Get this powder 0.5g and join in the ascorbic acid solution that 20mL concentration is 30mg/L, vibration 15min, precipitate and separate, deionized water rinsing, nitrogen protection oven dry down; The powder particle that obtains is joined in the 50mL methylene blue solution, and regulating pH is 1, vibration 30min; Add 4mL concentration again and be 30% H
2O
2, auxiliary with ultra-sonic oscillation 30min, organism is fully degraded.Remaining methylene blue concentration in the centrifugation analytical solution, result show that the clearance of methylene blue is 95.3%.
Embodiment 2
60 purpose powder are pulverized and be milled into to volcanics; Get this powder 2g and join in the ascorbic acid solution that 20mL concentration is 100mg/L, vibration 20min, precipitate and separate, deionized water rinsing, nitrogen protection oven dry down; The powder particle that obtains is joined in the orange II waste water of 50mL dyestuff, and regulating pH is 6, vibration 30min; Add 0.1mL concentration again and be 30% H
2O
2, auxiliary with ultra-sonic oscillation 1h, organism is fully degraded, remaining orange II concentration in the centrifugation analytical solution, the result shows that the clearance of orange II is 99.07%.
Embodiment 3
50 purpose powder are pulverized and be milled into to volcanics; Get this powder 1g and join in the ascorbic acid solution that 20mL concentration is 60mg/L, vibration 18min, precipitate and separate, deionized water rinsing, nitrogen protection oven dry down; The powder particle that obtains is joined in the 50mL phenolic waste water, and regulating pH is 3, vibration 30min; Add 2mL concentration again and be 30% H
2O
2, auxiliary with ultra-sonic oscillation 50h, organism is fully degraded, remaining naphthalene concentration in the centrifugation analytical solution, result show that the clearance of phenol is 98.9%.
Claims (2)
1. the treatment process of an organic waste water is characterized in that: in turn include the following steps:
(1) 10～60 purpose powder are pulverized and be milled into to volcanics;
(2) get this powder 0.5～2g and join in the ascorbic acid solution that 20mL concentration is 30～100mg/L, vibration 15～20min, precipitate and separate, deionized water rinsing, nitrogen protection oven dry down;
(3) powder particle that obtains is joined in the 50mL organic waste water, regulating pH is 1～6, vibration 30min;
(4) adding 0.1～4mL concentration is 30% H
2O
2, auxiliary with ultra-sonic oscillation 30min～1h, organism is fully degraded get final product.
2. the treatment process of a kind of organic waste water according to claim 1, it is characterized in that: described volcanics is a basalt.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200910234358XA CN101708886B (en) | 2009-11-24 | 2009-11-24 | Method for treating organic waste water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200910234358XA CN101708886B (en) | 2009-11-24 | 2009-11-24 | Method for treating organic waste water |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101708886A CN101708886A (en) | 2010-05-19 |
| CN101708886B true CN101708886B (en) | 2011-07-27 |
Family
ID=42401698
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200910234358XA Active CN101708886B (en) | 2009-11-24 | 2009-11-24 | Method for treating organic waste water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101708886B (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| IL207783A0 (en) * | 2010-08-24 | 2010-12-30 | Boaz Shitzer | Enhanced advanced oxidation procedure |
| CN103521242A (en) * | 2012-07-03 | 2014-01-22 | 中国石油化工股份有限公司 | Heterogeneous catalysis wet oxidation catalyst taking volcanic rock as carrier and preparation method thereof |
| CN103496781A (en) * | 2013-10-28 | 2014-01-08 | 武汉大学 | Method of organic wastewater treatment through persulfate activation |
| CN104176813B (en) * | 2014-08-29 | 2016-06-22 | 四川航天拓鑫玄武岩实业有限公司 | Fenton reagent preparation method |
| CN104826390A (en) * | 2015-04-21 | 2015-08-12 | 安徽凤凰滤清器股份有限公司 | Modified volcanic rock absorption filtering agent, and preparation method thereof |
| CN104923155A (en) * | 2015-05-21 | 2015-09-23 | 安徽凤凰滤清器股份有限公司 | Desulfurizer adsorbent and preparation method thereof |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101134609A (en) * | 2007-08-07 | 2008-03-05 | 江苏工业学院 | Method for processing organic wastewater by employing ultrasonic wave and synergic organophilic bentonite |
| CN101269869A (en) * | 2008-04-29 | 2008-09-24 | 江苏工业学院 | Processing method for phosphor containing wastewater |
| CN101314487A (en) * | 2008-06-12 | 2008-12-03 | 江苏工业学院 | Method for removing cation type dye in printing and dyeing wastewater |
-
2009
- 2009-11-24 CN CN200910234358XA patent/CN101708886B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101134609A (en) * | 2007-08-07 | 2008-03-05 | 江苏工业学院 | Method for processing organic wastewater by employing ultrasonic wave and synergic organophilic bentonite |
| CN101269869A (en) * | 2008-04-29 | 2008-09-24 | 江苏工业学院 | Processing method for phosphor containing wastewater |
| CN101314487A (en) * | 2008-06-12 | 2008-12-03 | 江苏工业学院 | Method for removing cation type dye in printing and dyeing wastewater |
Non-Patent Citations (1)
| Title |
|---|
| JP特开2007-117784A 2007.05.17 |
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