CN100503475C - Method for treating arsenic waste solution of hazardous waste by using composite functional bacteria - Google Patents
Method for treating arsenic waste solution of hazardous waste by using composite functional bacteria Download PDFInfo
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- CN100503475C CN100503475C CNB2007100486753A CN200710048675A CN100503475C CN 100503475 C CN100503475 C CN 100503475C CN B2007100486753 A CNB2007100486753 A CN B2007100486753A CN 200710048675 A CN200710048675 A CN 200710048675A CN 100503475 C CN100503475 C CN 100503475C
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- 238000000034 method Methods 0.000 title claims abstract description 36
- 239000002131 composite material Substances 0.000 title claims abstract description 16
- 229910052785 arsenic Inorganic materials 0.000 title claims description 118
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 title claims description 117
- 239000002699 waste material Substances 0.000 title claims description 61
- 239000002920 hazardous waste Substances 0.000 title claims description 14
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- 238000001556 precipitation Methods 0.000 claims abstract description 8
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- 229910052742 iron Inorganic materials 0.000 claims abstract description 5
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Landscapes
- Removal Of Specific Substances (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Abstract
This invention discloses a method for treating dangerous As-containing wastewater with composite functional bacteria. The composite functional bacteria are obtained by: mixing Desulfovibrio Sp., Desulfotomaculum Sp. and Bacillus megaterium Sp. at a number ratio of (20-65):(15-55):(5-10), and culturing in a culture medium containing Fe, S, C, N and P in anaerobic environment at 30-37 deg.C and pH 7.0-7.4 for 33-38 h. The method comprises: adding the composite functional bacteria and As-containing wastewater (pH = 2.5-9.0, and As concentration = 0.7-6140 mg/L) at a volume ratio of (1-6):1000 into a bioreactor, mixing, stirring for 5-60 min, precipitating in a precipitation pool, and filtering. The method has such advantages as simple process, short treatment period, small floor area, low energy consumption, and no secondary pollution.
Description
Technical field
The invention belongs to the liquid waste disposal technique field, especially belong to and adopt compound function yeast to handle the method that Hazardous wastes contains arsenic waste solution (waste water).
Background technology
Contain arsenic (As) and arsenic compound refuse and belong to hypertoxic Hazardous wastes.Trivalent arsenic (As
3+) toxicity than pentavalent arsenic (As
5+) strong toxicity, the toxicity of inorganic arsenic is greater than organoarsenic.Being accumulated in intravital arsenic and compound thereof and having carcinogenic, teratogenesis, is 0.01～0.052g to people's toxic dose, and lethal quantity is 0.06～0.2g.The maximum permissible concentration of arsenic is 50ug/L in China's surface water; The maximum permissible concentration of arsenic is 10ug/L in state's tap water such as Europe, the United States, day.Because a large amount of exploitations, production and the use of arsenic, the pollution of arsenic is more and more serious.The arsenic-containing waste water that production processes such as mining, metallurgy, fire coal, chemical industry produce all can pollute environment.Soak as arsenopyrite that the arsenic more than 80% enters solution in the golden nitric acid catalysis, arsenic is up to 15～30g/L in its oxidation leach liquor.In recent years the environmental pollution accident that relevant arsenic waste solution produces happens occasionally: Guizhou Chemical-Ferdtilizer Factory in 2000 arsenic-containing waste water discharging causes downstream big area arsenic contamination to poison; Near the fishes and shrimps extinction in the field arsenic of Jiangyong County, Hunan in 2003 arsenic products factory makes, No kernels or seeds are gathered, as in a year of scarcity, over one hundred people poisoning of drinking water; The waste water straightly discharging in yueyang, hunan county great source chemical company in 2006 and Taolin Lead-zinc Mine chemical plant causes the high-wall river is polluted, and arsenic exceeds standard about 10 times.Environmental administration has carried out severe investigation to illegal enterprise in accordance with the law, the arsenic contamination troublemaker that detains, and investigated its Criminal Responsibility in accordance with the law.As seen, very urgent to the effective improvement that contains arsenic waste solution.
The method of handling arsenic-containing waste water has physics, chemistry and biological process.The physics method needs a large amount of sorbent materials, and sorbent material is more expensive, the regeneration difficulty; Chemical method need be with a large amount of chemical reagent.These two kinds of equal efficient of method are low, the cost height, and easily cause secondary pollution.
The research that existing biological process is handled arsenic-containing waste water has following report: people such as Suhendrayatna have studied the conversion of chlorella to arsenic, and the enrichment that records arsenic can reach the 610ug/g cell.Weger etc. get a strain bacterium (ULPAs1) from arsenic-containing waste water can be at As
3+1.33mmol/L grow in the substratum (100mg/L), minimum inhibitory concentration is 500mg/L.Green sieves a strain bacterium (Bacillusarsenoxidans) from livestock dipping bath water, can be with As
3+Be oxidized to As
5+Gihring etc. tell the ThermusHR13 bacterium at high arsenic geothermal environment also can be with As
3+Be oxidized to As
5+People such as the Anderson arsenic oxydase of from alcaligenes faecalis (Alcaligenesfaecalis), having purified.Mokashi and Paknikar be As in coryneform bacteria (Microbacterium Lacticum) the oxidation underground water fixedly
3+, with the active carbon adsorption arsenic removal effect is preferably arranged again.Silver etc. point out arsenus acid to be oxidized to arsenic acid under the effect of molybdoprotein enzyme and ferritin enzyme.
Summary of the invention
The method that the purpose of this invention is to provide a kind for the treatment of arsenic waste solution of hazardous waste by using composite functional bacteria, this method technology is simple, and the treatment time is short, and occupied ground is few, and energy consumption is little, and cost is low, and non-secondary pollution can be handled the High Concentration of Arsenic waste liquid, realizes qualified discharge.
The present invention realizes that the technical scheme that its goal of the invention adopts is: a kind of method for the treatment of arsenic waste solution of hazardous waste by using composite functional bacteria the steps include:
A, bacterial strain are selected and proportioning: compound function yeast is made up of desulfovibrio (Desulfovibrio Sp.), desulfurization intestines shape bacterium (Desulfotomaculum Sp.), bacillus megaterium (Bacillus megaterium Sp.), and the bacterium of three strain bacterium is counted ratio and is: 20～65:15～55:5～10;
B, compound function yeast cultivate: three kinds of bacterial classifications in A step are counted ratio by its strain, cultivate culture condition with the nutrition that contains Fe, S, C, N, P composition in the cultivation device: anaerobic environment, pH7.0～7.4,30～37 ℃, incubation time 33～38 hours;
C, arsenic waste solution handle: B is gone on foot compound function yeast in the cultivation device and meta-bolites thereof, nutrition as the detoxification thing, with pH2.5～9.0, the arsenic waste solution that arsenic concentration 7～61400 grams are/10 cubic metres is by the volume ratio of 1～6:1000, enter to mix in the bio-reactor and stir, reacted 5～60 minutes, again through the settling tank precipitate and separate, strainer filters, and isolates mud and discharge water.
The mechanism that compound function yeast of the present invention is removed arsenic is:
One, three kinds of bacterium in the compound function yeast: desulfovibrio (Desulfovibrio Sp.), desulfurization intestines shape bacterium (Desulfotomaculum Sp.), bacillus megaterium (Bacillus megaterium Sp.) can be with the As in the arsenic waste water
3+Be oxidized to As
5+After, arsenic can also be methylated.Oxidation and methylated arsenic are enriched in the thalline shell, enter in the thalline on a small quantity.The methyl arsenic that produces after methylating, the toxicity of dimethyl arsenic, arsenous methide is more much lower than inorganic arsenic, and can be precipitated at settling tank.Therefore, compound function yeast is to the process of water body arsenic enrichment, also is one the process of malicious detoxification fallen in arsenic, makes the present invention to carry out the arsenic waste solution of concentration up to the high density of 6140mg/L.
Two, owing to contain Fe, S composition in the nutrition, in compound function yeast survival in the cultivation device, growth, the reproductive process, can produce some meta-bolitess: as Fe
2+, Fe
3+, S
2-Deng, the arsenous anion (AsO in these meta-bolitess and the arsenic waste solution
- 2) and arsenate (AsO
3- 4) reaction, generate ferrous arsenate and ferric arsenate precipitation, that is:
2AsO
3- 4+6Fe
2+＝2Fe
3(AsO
4)
2↓
AsO
3- 4+Fe
3+＝FeAsO
4↓
Other meta-bolites such as SO
2Deng having an oxidisability, can oxidation As
3+Be As
5+, the As in the arsenic waste solution
3+Be oxidized to As
5+After, also can with Fe
2+, Fe
3+(ferrous arsenate is 10 in the solubleness of 25 ℃ of water to generate ferrous arsenate and ferric arsenate precipitation
-6Mol/L.The solubility product of ferric arsenate in 25 ℃ of water is 5.7 * 10
-21)).The above chemical reaction reaction times is short, general 3～25 minutes.
Chemical action by biomagnification and meta-bolites.The inventive method can be removed the arsenic in the High Concentration of Arsenic waste liquid effectively and quickly, realizes the processing to arsenic waste solution of hazardous waste.
Compared with prior art, the invention has the beneficial effects as follows:
Multiple effects such as the absorption of the composite bacteria that the present invention becomes by optimum combination and the oxidation of meta-bolites thereof, thalline, flocculation, precipitation have reduced the residual quantity of arsenic in the arsenic waste solution to greatest extent.Experiment showed, the discharge water after the inventive method is handled, arsenic content reaches GB GB8978-1996 " integrated wastewater discharge standard " first discharge standard, and the content of arsenic is less than 0.5mg/L, thereby realization is to the processing of the useless waste water of High Concentration of Arsenic.In treating processes, the detoxification thing is microorganism and metabolite thereof, does not add harmful chemical, does not produce secondary pollution, can be widely used in the various processing that contain arsenic waste solution (waste water) in the Industrial processes.
Three strain bacterium of employing of the present invention are known bacterial strain, and it is simple that it cultivates the preparation method; The biological detoxication of compound function yeast, the oxidation of falling poison and meta-bolites and precipitin reaction detoxification process, normal temperature carries out in bio-reactor, and the reaction times is short, is no more than 60 minutes, and occupied ground is few, and energy consumption is little, and cost is low.
Composite bacteria is cultivated in special-purpose incubator, has prevented the heritable variation of bacterium, and cultured bacterium can be standby at any time, and is very convenient.
And, in the waste liquid if having other heavy metal ion such as a Zn
2+, Cu
2+, Cr
3+, Ni
2+, Cd
2+Can be adsorbed by composite bacteria of the present invention Deng also, remove through flocculation sediment again.
When the arsenic waste solution in above-mentioned C step was handled, arsenic concentration 0.7～200mg/L, bio-reactor were the one-level bio-reactor, and the reaction times 5～30 is minute that settling tank is the one-level settling tank.
When arsenic concentration is low, only need first order reaction and precipitation, arsenic waste solution can be handled up to standard through the short time.
When the arsenic waste solution in above-mentioned C step was handled, arsenic concentration 201～6140mg/L, bio-reactor were the I and II bio-reactor, and every order reaction time 5～30 is minute that settling tank should be the I and II settling tank mutually.
For the High Concentration of Arsenic waste liquid of 201～6140mg/L, process second order reaction and precipitation can realize the qualified discharge of arsenic waste solution.
With the settling tank precipitation in above-mentioned C step obtain with strainer in the mud that leaches take out, add sulfuric acid and heating for dissolving after, cooling, crystallization more promptly gets white arsenic (As with the xln washing
2O
3) product, and lysate is as the raw material that reclaims Zn, Cu, Ni, remaining body refuse is made building materials.
Above-mentioned vitriolic concentration 80～98%, the volume ratio of sulfuric acid and mud are 5～7:1, and 170 ℃～190 ℃ were heated 2-3 hour.
Like this, the present invention can be recycled the arsenic of enrichment in the mud and zinc, copper, nickel, and body refuse is made building materials, makes the innoxious and resource utilization of arsenic waste solution of hazardous waste.Have good economic benefit and environmental benefit.
The characteristic of the three strain bacterium that the present invention adopts is as follows:
One, desulfovibrio (Desulfovibrio sp.)
Size: 0.5-1 * 3-5 μ m, shape: crooked shaft-like.
Feature: with the flagellar movement of extremely singly growing thickly, no gemma and pod membrane, Gram-negative.
Physiological characteristic: organic chemoheterotrophic bacteria is H with anaerobic respiration reduced sulphur or other reducible sulphur compounds
2S obtains energy, utilizes lactic acid salt, pyruvate salt, and malate, oxidable to acetate, not aerogenesis.Cell contains C
3Cytopigment and desulfovibrio element.Absorption peak 630 nanometers.Oxydase is arranged.Liquefy gelatin does not reduce nitrate, anaerobic growth, and 5-44 ℃ of growth temperatures, 25-30 ℃ of optimum tempss, best pH7.2, G+C61.2 ± 1% mol, when pH7.2, the En of growth is-100mv.
Two, desulfurization intestines shape bacterium (Desulfotomaculum sp.)
Size: 0.3-1.5 * 3-6um, shape: shaft-like end garden is the grape chain sometimes.
Feature: peritrichous motion, spore ovum garden shape, Gram-negative.In the lactic acid salt of ferrous salt-vitriol substratum is arranged, produce the bacterium colony of black.
Physiological characteristic: chemoorganotrophy, respiratory metabolism vitriol, sulphite and reducible sulfur compound play the electronics acceptor and are reduced into H
2S.Do not utilize carbohydrate, not oxidation acetate, incomplete oxidation organic substrates cause acetate or homologue and CO
2Formation.Cell contains the cytopigment of protoheme class.Anaerobic growth, 30-42 ℃ of growth temperatures, 30-37 ℃ of optimum temperutures, optimal pH 6-7, to the people, cavy, big small white mouse and rabbit are not pathogenic.The G+C content of DNA is 45.6 ± 1% mol.
Three, bacillus megaterium (Bacillus megaterium Sp.)
Size: 0.8-2.5 * 3-5um
Shape: direct rod shape, often with paired or catenation, tool nose circle or square end.
Feature: the cell dyeing Gram-positive presents Gram-positive or feminine gender when the children cultivates age.Move with peritrichous.Gemma ellipse, cylindricality, circle can resist many poor environments.Each cell produces a gemma, gives birth to spore and is not suppressed by oxygen.
Physiological characteristic: the energy heterotrophic bacteria that organises, amphimicrobian has the resistance to heat, pH and salt poor environment, 10～30 ℃ of growth temperatures, pH6～7.Utilize the substrate respiratory metabolism, the long-time cultivation, grower turns black, and the catalase positive is produced acid from pectinose, wood sugar and N.F,USP MANNITOL, liquefy gelatin fast (22 ℃), casein is cleared up rapidly, assimilation nitrate, but do not accumulate nitrite.Under no growth factor, can be carbon nitrogen source propagation with ammonium salt, nitrate and glucose.The G+C content of DNA is the 36-38 mol.Separation is from organic phosphorus bacteria fertilizer.
The present invention is described in further detail below in conjunction with accompanying drawing and concrete embodiment.
Description of drawings
Fig. 1 is the process flow diagram of the embodiment of the invention.
Embodiment
Embodiment one
Fig. 1 illustrates, and a kind of embodiment of the present invention is: a kind of method for the treatment of arsenic waste solution of hazardous waste by using composite functional bacteria the steps include:
A, bacterial strain are selected and proportioning: compound function yeast is made up of desulfovibrio (Desulfovibrio Sp.), desulfurization intestines shape bacterium (Desulfotomaculum Sp.), bacillus megaterium (Bacillus megaterium Sp.), and the bacterium of three strain bacterium is counted ratio and is: 60:50:8.
B, compound function yeast are cultivated: three kinds of bacterial classifications in A step are counted ratio by its strain, cultivate culture condition: anaerobic environment, 30 ℃ of pH7.0, temperature, incubation time 36 hours with the nutrition that contains Fe, S, C, N, P composition in the cultivation device.
C, arsenic waste solution is handled: B is gone on foot compound function yeast and meta-bolites thereof in the cultivation device, nutrition is as the detoxification thing, with pH0.76～1.15, arsenic waste solution (and the chloride ion-containing of arsenic concentration 226.5～4518.4 mg/litre, pollutents such as washing composition), volume ratio by 4～5.5:1000, enter to mix in the one-level bio-reactor and stir, reaction times 15～25 is minute, through one-level settling tank post precipitation, supernatant liquor enters the two stage biological reactor, reaction 15～25 is minute, through the second-level settling pond post precipitation, supernatant liquor filters through filter again, isolates mud and discharge water.After testing, As content is lower than 0.05mg/L in the discharge water, reaches the first discharge standard of GB GB8978-1996 " integrated wastewater discharge standard ".
Simultaneously the mud in I and II settling tank and the strainer is taken out and deposit in the sludge sump.When mud is recycled, the mud in the sludge sump is taken out, puts into reactor, add 90% sulfuric acid of 6 times of sludge volumes, be heated to 180 ℃ with mud dissolving 2.5 hours, solution cools off again, crystallization, and the xln washing promptly gets white arsenic (As
2O
3) product, and lysate further reclaims as the raw material that reclaims Zn, Cu, Ni, remaining body refuse is made building materials.
The arsenic waste solution that contains that this example is handled is that certain company produces the arsenic waste solution of its pH0.45～1.60 in actual production process.Because high acidity (pH≤2) has infringement to thalline, for preventing of the decomposition of high acidity, before handling, need in arsenic waste solution, to add milk of lime earlier with compound function yeast to thalline, regulate its pH to 2.5～4, handle again.
Fig. 1 illustrates, the technical process of present embodiment and corresponding container are: the waste liquid that gives off in the production is stored in earlier in the waste liquid equalizing tank, in the waste liquid equalizing tank in arsenic waste solution and the cultivation device detoxification thing such as cultured compound function yeast enter and react in the one-level bio-reactor, enter one-level settling tank post precipitation then, supernatant liquor enters the two stage biological reactor reaction, through the second-level settling pond post precipitation, supernatant liquor enters strainer and filters, and clear water is qualified discharge water and externally discharges.Simultaneously, be the conserve water resource, the clear water in the strainer also has part to flow in the culture groove as reuse water, for the culture utilization.Mud in I and II settling tank and the strainer is stored in the sludge sump after the taking-up.When mud is recycled, the mud in the sludge sump is taken out, put into reactor, simultaneously sulfuric acid is added in the reactor, reclaim metals such as extraction white arsenic product and zinc, copper, nickel.Body refuse is made building materials and is used.
Following table is the processing monitoring result (annotating: because of this contains arsenic waste solution acidity height, before compound function yeast enters A reactor, add milk of lime earlier to regulate its acidity to pH2.5～4) of present embodiment:
Embodiment two
This example and embodiment one are basic identical, different only be:
The bacterium of compound function yeast desulfovibrio (Desulfovibrio Sp.), desulfurization intestines shape bacterium (DesulfotomaculumSp.), bacillus megaterium (Bacillus megaterium Sp.) three strain bacterium is counted ratio and is: 56:55:10.Culture condition: anaerobic environment, 37 ℃ of pH7.4, temperature, incubation time 38 hours; The arsenic waste solution of the pH2.5 of arsenic waste solution～3, arsenic concentration 5662～6140 mg/litre, detoxification thing that by compound function yeast is and arsenic waste solution be by the volume ratio of 5.6～6:1000, enter mix in the I and II bio-reactor stir, every order reaction 20～30 minutes.The 170 ℃ of heats of solution of 85% sulfuric acid 3 hours that add 5 times of volumes in the mud, reclaim As
2O
3Product.The rate of recovery 97% of arsenic.
Discharge water is through monitoring, and arsenic content is 0.05mg/L in the discharge water, pH8.5.Total arsenic in the discharge water and pH are better than the first discharge standard of GB GB8978-1996.
Embodiment three
This example and embodiment one are basic identical, different only be:
The bacterium number of compound function yeast desulfovibrio (Desulfovibrio Sp.), desulfurization intestines shape bacterium (DesulfotomaculumSp.), bacillus megaterium (Bacillus megaterium Sp.) three strain bacterium is than being 41:38:5.Culture condition: anaerobic environment, 31 ℃ of pH7.1, temperature, incubation time 32 hours; With pH7.8～9.0 in certain copper mine workshop, the arsenic waste solution of arsenic concentration 201～1765.1 mg/litre, per hour handle 4m with the inventive method
3Arsenic waste solution.Volume ratio by compound function yeast master's detoxification thing and arsenic waste solution are pressed 4～5:1000 enters in the I and II bio-reactor and mixed stirring, first order reaction 5 minutes, second order reaction 30 minutes.As content 8.0% reclaims As with sulfuric acid process in the mud, adds 95% sulfuric acid of 6.5 times of volumes, 180 ℃ of heats of solution 3 hours in the mud, As
2O
3206.2kg/t dewatered sludge, the As rate of recovery 97.3%.Discharge water is monitored through the random sampling of environmental monitoring junction centre: pH6.4～8.9, average 7.65, arsenic 0.01～0.05mg/L, average 0.03mg/L.Total As of discharge water and pH are better than the first discharge standard of GB GB8978-1996.
Embodiment four
This example and embodiment one are basic identical, different only be:
The bacterium number of compound function yeast desulfovibrio (Desulfovibrio Sp.), desulfurization intestines shape bacterium (DesulfotomaculumSp.), bacillus megaterium (Bacillus megaterium Sp.) three strain bacterium is than being 20:55:5.Culture condition: anaerobic environment, 31 ℃ of pH7.1, temperature, incubation time 35 hours; The arsenic-containing waste water of certain sulfuric acid subsidiary factory of chemical industry group company: pH2.5 contains As 17.9-71.4mg/L, F 15.7～103.0mg/L, Pb
2+, Cu
2+, Zn
2+, Cd
2+Deng trace (being lower than the first discharge standard of GB GB8978-1996).
Because arsenic content is low in this routine arsenic waste solution, the arsenic content when the highest also only is 71.4mg/L, therefore only need carry out first order reaction and get final product.By the volume ratio that compound function yeast master's detoxification thing and arsenic waste solution are pressed 2.7～3.4:1000, enter to mix in the one-level bio-reactor and stir, reacted 10～30 minutes, precipitate through the one-level settling tank again, ultimate filter can be realized qualified discharge after filtering.
Reclaim As with sulfuric acid process, add 80% sulfuric acid of 5.5 times of volumes, 170 ℃ of heats of solution 2 hours in the mud, As
2O
351.6kg/t dewatered sludge, the As rate of recovery 97.2%.Discharge water is monitored through the random sampling of environmental monitoring junction centre: pH7.2, and As 0.04mg/L, F 0.2mg/L, Pb, Cu, Zn, Cd do not detect.Water outlet pH, As, F are better than the first discharge standard of GB GB8978-1996.
Embodiment five
This example and embodiment one are basic identical, different only be:
The bacterium of compound function yeast desulfovibrio (Desulfovibrio Sp.), desulfurization intestines shape bacterium (DesulfotomaculumSp.), bacillus megaterium (Bacillus megaterium Sp.) three strain bacterium is counted ratio and is: 29:15:5.Culture condition: anaerobic environment, 37 ℃ of pH7.4, temperature, incubation time 33 hours; The arsenic-containing waste water of certain fertilizer plant: pH5～7.6 contain As 3.31～200mg/L.This routine arsenic content is low, need carry out first order reaction with four the same of embodiment.By the volume ratio that compound function yeast master's detoxification thing and arsenic waste solution are pressed 1.8～4:1000, enter to mix in the one-level bio-reactor and stir, reacted 5～10 minutes.Reclaim As with sulfuric acid process, add 90% sulfuric acid of 6.8 times of volumes, 190 ℃ of heats of solution 3 hours in the mud.
Discharge water the results are shown in following table through environmental monitoring junction centre random sampling monitoring.
The pH fluctuation of discharge water is 6.03～7.52, and As fluctuates at 0.01～0.02mg/L, is better than the first discharge standard of GB GB8978-1996.
Embodiment six
This example and embodiment one are basic identical, different only be:
The bacterium of compound function yeast desulfovibrio (Desulfovibrio Sp.), desulfurization intestines shape bacterium (DesulfotomaculumSp.), bacillus megaterium (Bacillus megaterium Sp.) three strain bacterium is counted ratio and is: 65:48:5.Culture condition: anaerobic environment, 35 ℃ of pH7.4, temperature, incubation time 33 hours; With pH6.5～7.5 in certain copper mine workshop, the arsenic waste solution of arsenic concentration 0.7～20 mg/litre,, enter to mix in the one-level bio-reactor and stir, reacted 5～20 minutes by the volume ratio that compound function yeast master's detoxification thing and arsenic waste solution are pressed 1～2.7:1000.This routine arsenic content is low, also only need carry out first order reaction with embodiment four is the same.Add 98% sulfuric acid of 7 times of volumes, 190 ℃ of heats of solution 2 hours in the mud, reclaim As
2O
3Product.The rate of recovery is: the As15.1kg/t dewatered sludge.
Also contain Zn 4.5～20.0mg/L, Ni 3.0～14.2mg/L and Cu49～140mg/L in the arsenic waste solution in this example simultaneously.After this law is handled, recyclable obtaining: Zn 10.5kg/t dewatered sludge, Ni 4.4kg/t dewatered sludge, Cu 33.8kg/t dewatered sludge.Discharge water after the processing carries out continuous 10 batch monitoring result with the TCP-AES instrument to discharge water through this environmental monitoring station: As 0.01～0.05mg/L, Zn
2+0.01～0.16mg/L, Ni
2+0.15～0.47mg/, Cu 0.01～0.15mg/L, pH6.5～8.4.As, Zn, Ni, Cu and pH all are better than the first discharge standard of GB GB8978-1996.
Because high acidity (pH≤2) has infringement to thalline,, when handling arsenic waste solution,, add compound function yeast again and handle if the pH that contains arsenic waste solution (waste water) must transfer to 3～4 with pH with milk of lime below 2 with the inventive method for preventing of the decomposition of high acidity to thalline.
When the inventive method was handled arsenic waste solution, the concentration of arsenic waste solution was high more, and the compound function yeast of adding is also many more, and the reaction times also extends.To the processing of certain arsenic waste solution of actual discharge, the compound function yeast of adding and reaction times can be determined by simple test several times.
Claims (5)
1, a kind of method for the treatment of arsenic waste solution of hazardous waste by using composite functional bacteria the steps include:
A, bacterial strain are selected and proportioning: compound function yeast is made up of desulfovibrio (Desulfovibrio Sp.), desulfurization intestines shape bacterium (Desulfotomaculum Sp.), bacillus megaterium (Bacillus megaterium Sp.), and the bacterium of three strain bacterium is counted ratio and is: 20～65:15～55:5～10;
B, compound function yeast cultivate: three kinds of bacterial classifications in A step are counted ratio by its bacterium, cultivate culture condition with the nutrition that contains Fe, S, C, N, P composition in the cultivation device: anaerobic environment, pH7.0～7.4,30～37 ℃, incubation time 33～38 hours;
C, arsenic waste solution handle: B is gone on foot compound function yeast in the cultivation device and meta-bolites thereof, nutrition as the detoxification thing, with pH9.0～2.5, the arsenic waste solution of arsenic concentration 0.7～6140 mg/litre is pressed 1～6: 1000 volume ratio, enter to mix in the bio-reactor and stir, reacted 5～60 minutes, again through the settling tank precipitate and separate, strainer filters, and isolates mud and discharge water.
2, the method for a kind for the treatment of arsenic waste solution of hazardous waste by using composite functional bacteria according to claim 1, it is characterized in that: when the arsenic waste solution in described C step is handled, arsenic concentration 0.7～200mg/L, bio-reactor is the one-level bio-reactor, reaction times is 5～30 minutes, and settling tank is the one-level settling tank.
3, the method for a kind for the treatment of arsenic waste solution of hazardous waste by using composite functional bacteria according to claim 1, it is characterized in that: when the arsenic waste solution in described C step is handled, arsenic concentration 201～6140mg/L, bio-reactor is the I and II bio-reactor, every order reaction time is 5～30 minutes, and settling tank should be the I and II settling tank mutually.
4, the method for a kind for the treatment of arsenic waste solution of hazardous waste by using composite functional bacteria according to claim 1, it is characterized in that: with the settling tank precipitation in described C step obtain with strainer in the mud that leaches take out, after adding sulfuric acid and heating for dissolving, cooling, crystallization again, the xln washing is promptly got the white arsenic product, and lysate is as the raw material that reclaims Zn, Cu, Ni, and remaining body refuse is made building materials.
5, the method for a kind for the treatment of arsenic waste solution of hazardous waste by using composite functional bacteria according to claim 4 is characterized in that: described vitriolic concentration 80～98%, the volume ratio of sulfuric acid and mud are 5～7:1, and 170 ℃～190 ℃ were heated 2-3 hour.
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| CN102344214B (en) * | 2011-08-01 | 2012-10-17 | 浙江大学 | Physicochemical comprehensive treatment system for dangerous waste liquid |
| CN103540525A (en) * | 2012-07-08 | 2014-01-29 | 安徽阜阳永志环能工程有限公司 | Double-level anaerobic tower |
| CN105060620B (en) * | 2015-07-26 | 2017-05-31 | 杭州英普环境技术股份有限公司 | It is a kind of to remove the method containing arsenic wastewater pollutants |
| CN107162215B (en) * | 2017-06-13 | 2020-07-24 | 江苏康爱特环境工程集团有限公司 | Biochemical process for treating arsenic-containing wastewater |
| CN107399807A (en) * | 2017-07-31 | 2017-11-28 | 青岛海澄知识产权事务有限公司 | A kind of method that arsenic-containing waste water is repaired using sludge |
| CN109133362A (en) * | 2018-08-06 | 2019-01-04 | 中国地质大学（武汉） | A kind of construction method of acidproof arsenic oxidizing bacteria group biofilm reactor and application |
| WO2020211024A1 (en) * | 2019-04-18 | 2020-10-22 | 华南师范大学 | Method for removing trivalent arsenic and pentavalent arsenic in acidic arsenic-containing wastewater |
| CN110373544B (en) * | 2019-07-25 | 2020-06-16 | 中国科学院过程工程研究所 | Device and method for gradient treatment of metal ions in heavy metal sludge by deep-sea microorganisms |
| CN112063385B (en) * | 2020-09-16 | 2021-04-30 | 南京大学 | Passivating agent for efficiently fixing trivalent arsenic under anaerobic condition, and preparation method and application thereof |
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