CN100999344A - Multistage gradient adsorption channel adsorption technology - Google Patents
Multistage gradient adsorption channel adsorption technology Download PDFInfo
- Publication number
- CN100999344A CN100999344A CNA2006100456359A CN200610045635A CN100999344A CN 100999344 A CN100999344 A CN 100999344A CN A2006100456359 A CNA2006100456359 A CN A2006100456359A CN 200610045635 A CN200610045635 A CN 200610045635A CN 100999344 A CN100999344 A CN 100999344A
- Authority
- CN
- China
- Prior art keywords
- adsorption
- water
- gradient
- adsorption column
- technology
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Images
Classifications
-
- 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
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Abstract
This invention relates to adsorbing technology that uses adsorptive process for processing various kinds of waste water. Concretely it is many-stage grade adsorption tank adsorbing technology. Use many-stage dissymmetry U type pillar as adsorbing substance packing pillar, use adsorbing substance as packing material. After achieving adsorptive capacity, reclaim heavy metals and regenerative adsorbing substance. This invention uses cheap adsorbing substance as packing material. Procedure is simple. Operation is stable and reliable. It is suitable for different heavy metal waste water disposal. Compared with existing vertical adsorbing column technology, its motive power is low. Cost is low. Passed waste water is more. Effect is good. Economic performance is good.
Description
Technical field
The present invention relates to heavy metal containing wastewater treatment, specifically a kind of multistage gradient adsorption channel adsorption technology based on natural low-cost sorbent.
Background technology
Heavy metal wastewater thereby is mainly derived from the industrial trade of mine metallurgy industry, mechanical workout trade effluent and other heavy metal-containing waste waters.All there is heavy metal contamination in the waste water of many factories, as mining factory, smelting factory, hardware source mill, plating factory, tannery etc., soil around some military base is also contaminated, even the concentration of heavy metal ion of some refuse landfill subsurface infiltration liquid exceeds standard.Along with rapid economy development, the waste water that contains heavy metal discharges in a large number, these kinds metal such as cadmium, lead, copper, zinc, chromium (trivalent and sexavalence), nickel, mercury, arsenic, gold and silver etc. enter in the surrounding environment in a large number, make underground water and surface water that contaminated by heavy metals danger be arranged.These heavy metals can not be accumulated in environment easily by biological decomposition, if enter food chain, will accumulate in living organism, cause various danger and disease.The economic worth of some heavy metal own is very high simultaneously, need recycle from waste water.Therefore, imperative for the processing of the heavy metal wastewater thereby in the various industrial trades.
Improvement technology to metallic pollution waste water comprises chemical precipitation, membrane filtration, ion-exchange, carbon absorption and precipitation absorption.It is very necessary using method and the material of effectively administering heavy metal contamination sewage.But some method is not suitable for a large amount of high densitys, component complexity, heavy metal wastewater thereby (as mine, smeltery, large-scale plating shop etc.) that quantity is big, and reason is that treatment process method complexity, inconvenient operation, capital construction, operation and maintenance cost are high.China is not so good to the water treatment effect in large-scale heavy metal mine, handles outside the reason of fund aspect, and also having a major reason is not have suitable treatment process or material.
The traditional technology of removing heavy metal ion in the trade effluent is a chemical precipitation method.By adding NaOH, lime or Na
2CO
3Regulate the pH of waste water, make the heavy metal ion in the waste water form precipitation, adopt subsequent techniques such as precipitation or filtration that throw out is separated with waste water then, thereby reach decontamination effect improving.Adopting alkaline precipitation is wherein modal technology, and traditional technology has following shortcoming: need device for dehydrating sladge waste; Floor space is big, complicated operation.The mud that traditional precipitator method produce is meeting stripping once again in neutrality or slightly acidic environment, causes secondary pollution.In addition, all there is certain defective in some process for treating heavy-metal waste water in actually operating, as for the heavy metal wastewater thereby with a large amount of complexing agents, can't handle with chemical precipitation method; Be impracticable or need the expense of great number for lower these methods of heavy metal wastewater thereby of concentration.Precipitation can only ease down to certain level to the dissolved metal concentration, the against regulation usually emission standard and the needs of further manufacturing procedure.And the financing requirement of increasing metal waste water control becomes maximum obstruction.Another difficult problem is that the treatment process of low-concentration heavy metal sewage is not infeasible economically, is exactly too complicated technically.
From technical feasibility, economical and efficient and environmental safety angle, research and develop a kind of environmental friendliness, novel treatment material that capital construction, operation and maintenance cost are low and the above-mentioned waste water of art breading that matches seem particularly important, in environment, accumulate guarantee environment safety to reduce or eliminate heavy metal.
Absorption method is a kind of method that is commonly used to handle heavy metal wastewater thereby, compares with additive method, and this method technology is simple, easy to operate, and capital construction, operation and maintenance cost are lower.With regard to expense, sorbent material price decision absorption method is handled the heavy metal wastewater thereby expense.Existing sorbent material such as sorbent materials such as gac, humic acids resin have stronger adsorptive power, the heavy metal removing rate height, but need to extract and preparation the cost height through industry.Seek focus cheap, that new adsorbent that adsorption activity is high (cost performance height) is just becoming heavy metal containing wastewater treatment.Price is an important parameter of comparison sorbent material.The expense of sorbent material changes with local available degree according to the needs of processing.Generally, if sorbent material need not process, abundanter at occurring in nature content, or the byproduct of other factory or waste, so just think cheap.Certainly also be remedying to the natural adsorbent modification to improve receptivity to processing charges.A large amount of available natural materialss and some industrial and agricultural production refuse all have the potential as low-cost sorbent.These material wide material sources, price cheapness are fit to apply.Needn't spend the substantial contribution manipulation of regeneration, greatly reduce the processing costs of heavy metal wastewater thereby.In recent years, many cheap novel absorption materials that adsorptive power is arranged have been reported both at home and abroad, as wilkinite, zeolite, medical stone, serpentine, many tuberculosis ore deposit, ocean, diatomite etc.Report to the heavy metal low-cost sorbent in the world wide mainly comprises: sweet peaceful, and chitin/chitosan, dead biology, sea grass/algae, xanthate, zeolite, diatomite, clay, mud coal soil, gelatine, humic acids, liver moss is by the sand after suitable modification or the modification, wool, cotton etc.The stronger natural materials of counterweight metal adsorption ability with report has: 1587mg Pb/g xylogen, 796mg Pb/g chitosan, 1123mg Hg/g chitosan, 1000mg Hg/g modification cotton, 92mg Cr (3)/g chitosan, 76mg Cr (3)/g, peat soil 558mg Cd/g chitosan, 215mg Cd/g sea grass.
The absorption potentiality of these low-cost sorbents and potential worldwide all have report.But it is rare really to say on a large scale that these low-cost sorbents are applied to the report of heavy metal wastewater thereby actual treatment.Its reason is:
1. although cheap on these natural adsorbent prices, loading capacity has been compared certain gap with traditional sorbent materials such as gacs.If still adopt the technology of traditional sorbent treatment heavy metal wastewater thereby, the advantage on the natural adsorbent price has been offset in the increase of expenses such as its treatment process operation and maintenance.
2. in the heavy metal containing wastewater treatment research at present, main research contents concentrates on the screening aspect to low-cost sorbent, but less to the absorbing process research that matches with low-cost sorbent.The large-scale application of existing absorbing process and the low-cost sorbent cover that mismatches also is the major reason of restriction low-cost sorbent development.
Summary of the invention
The object of the present invention is to provide a kind of economy, efficient, non-secondary pollution, environmentally friendly multistage gradient adsorption channel adsorption technology based on natural low-cost sorbent.
To achieve these goals, technical scheme of the present invention is as follows:
Comprise sorbent material pre-treatment → industrial sewage pre-treatment → upper prop absorption → subsequent treatment process, wherein sorbent material adopts natural low-cost sorbent in the sorbent material pre-treatment, particle is the 1-200 order, be that 4-10 is (except the chromate waste water with its pH regulator during the industrial sewage pre-treatment, it is 1-4.5 that the chromate waste water optimal adsorption is handled pH), sewage is removed suspended substance or particulate matter by sand filtration, precipitation before the upper prop absorption, and the adsorption column of employing is the multistage gradient adsorption column that contains a plurality of absorbing units; Each absorbing unit is made up of U type adsorption column, and wherein: the water inlet water level of single absorbing unit is higher than the water outlet water level.
Described natural low-cost sorbent is: sweet peaceful, peat, chitin or chitosan, dead biology, sea grass or algae, xanthate, zeolite, diatomite, clay, mud coal soil, gelatine, humic acids or liver moss.
Described sewage is based on heavy metal wastewater thereby, and taking second place is dyeing waste water.
The curved shape of the described U type adsorption column left side and the right pipe is asymmetric.The water inlet pipe height of next processing unit will be lower than a last unitary rising pipe height.Upper level processing unit and next stage processing unit mode of communicating can be for one to one or one-to-many, and promptly upper and lower level processing unit connects by network-like mode, utilize the multistage gradient of formation gravity flow of the self gravitation of waterhead and water.Water inlet will be higher than water outlet in the height of fill material.
When being reached capacity capacity, adsorbents adsorb reclaims noble metal behind the sorbent treatment noble metal described in the subsequent disposal of absorption mud with sour dissolution method.Can adopt simultaneously sludge dewatering, directly landfill, air-dry, burn and have the plant of super enrichment, rejection, tolerance to carry out biological restoration or biological fixation heavy metal.
The present invention has the following advantages:
1. cost is low.The present invention adopts cheap sorbent material, and the manufacture craft process is simple, and the adsorption column that adopts is a gravity flow, and it is low that gravity flow utilizes gravity to need not in adsorption process the consumption of power power consumption, compare the requirement of operation power with existing vertical-type adsorption column technology low, and working cost is low.
2. efficient height.The present invention adopts multiple-stage treatment, and treatment capacity is big, and the contraction in length sewage by reducing processing unit internal adsorption post can improve the treatment capacity in the unit time, and the sorbing material adsorptive power is strong by the time of adsorption column, and water outlet is effective.
3. flexible.The present invention can avoid the stopping state of adsorption column by sand filtration, intermediate processing removal suspended substance or particulate matter before absorption; Simultaneously also can to high density and low concentration heavy metal water obvious processing effect, adopt network-like mode to connect simultaneously, make things convenient for the maintenance and the renewal of absorbing unit at concentration of wastewater different adjustment processing units quantity.
4. green, environmental protection.The sorbent material that the present invention adopts is that natural product are environment friendly and pollution-free, and simultaneously treated sewage effect is up to state standards.
5. wide adaptability.The present invention is fit to following industry wastewater treatment: mining factory, smelting factory, hardware source mill, plating factory, tannery etc.; Processing all has better effects to heavy metal ion such as cadmium, lead, copper, zinc, chromium (trivalent and sexavalence), nickel, mercury, arsenic, gold and silver; To various single all effective with the mixture-metal ion waste water, adsorption conditions is less demanding.Single or broad variety heavy metal containing sewage all there is strong adsorption.
6. but the present invention's industrialization can be handled heavy metal wastewater thereby on a large scale.
7. market outlook are wide.Difficult point and emphasis in the harmless treatment water treatment industry of various concentration heavy metal trade effluents, the asymmetric U type of the unpowered multistage gradient adsorption column technology that is obtained by the present invention proposes a new technological line for this area treatment process, can be the time to the processing of heavy metal wastewater thereby, economic performance is good, compare with similar technology on the existing market, have stronger competitive power.
Description of drawings
Fig. 1 a is the tandem adsorption column structural representation of adsorption column technology in the prior art.
Fig. 1 b is the parallel adsorption column structural representation of adsorption column technology in the prior art.
Fig. 2 is an adsorption column structural representation of the present invention.
The atomic absorption spectrophotometry that Fig. 3 measures Cd for comparative example of the present invention detects figure.
The atomic absorption spectrophotometry that Fig. 4 measures Cd for one embodiment of the invention detects figure.
Embodiment
The present invention is described in more detail below by embodiment.
1. sorbing material pre-treatment
Sorbent material is: peat.Sorbent material is dried, pulverized particles 50 orders then, water is moistening when using then, and the back for the treatment of to absorb water fully is stand-by.
2. industrial sewage pre-treatment
The preparation of simulated wastewater: after the CaCl2 solid being dissolved into the distilled water of 1000mL, add the distilled water constant volume, being mixed with Cd concentration is 56.0mgL
-1Heavy metal solution, this moment pH be 6.The preparation of used simulated wastewater is identical therewith in the comparative example.
3. upper prop absorption
Adsorption column is: series connection gravity flow multistage gradient adsorption column (see figure 2), present embodiment adopts the asymmetric U type of tandem adsorption column, the high 3cm of adsorption column arranges from top to bottom, two adjacent column outlets link to each other with import, and single adsorption column water-in and water outlet difference of altitude are 1cm, and the water sample that comes out from a last outlet can directly enter next inlet and carrying out adsorption treatment like this.With fully the suction sorbing material be filled in the adsorption column, flow rate control at 5ml/h until reaching processing requirements.
4. subsequent disposal
Handle the sorbent material behind the noble metal, recycle noble metal in the sewage with sour dissolution method when its sorbent material reaches capacity capacity.Can adopt simultaneously sludge dewatering, directly landfill, air-dry, burn and have the plant of super enrichment, rejection, tolerance to carry out biological restoration or biological fixation heavy metal.
5. interpretation of result
The Cd of the water outlet General Logistics Department detects with atomic absorption spectrophotometry. and (as shown in Figure 4)
Embodiment 2: handle the trade effluent that contains heavy metal
1. sorbing material pre-treatment
Sorbent material is: through the natural adsorbent after the embedding modification be: chitin.Sorbent material is dried, pulverized particles 100 orders then, water is moistening when using then, and the back for the treatment of to absorb water fully is stand-by.
2. the pre-treatment of industrial sewage
Contain high density heavy metal industrial effluent--Wastewater from Acid Preparation, that wherein heavy metal content is the highest is Cd and Zn, and wherein the overwhelming majority is free state Cd and Zn. with 10% and 0.5%NaOH, amounts to 100mL and is adjusted to PH=9.0.Then the sewage that regulates is adopted the sedimentary method suspended substance that particle in the waste water is bigger.
| The useless former water pH water kind of industry | The heavy metal form | Cd(mg/L) | Pb(mg/L) | Cu(mg/L) | Zn(mg/L) |
| The relieving haperacidity 4.0-5.0 water that gives up | The total amount free state | 434.0±9.35 422.0±8.38 | 26.95±2.29 4.48±0.79 | 0.12±0.01 0 | 258.8±66.7 228.0±43.4 |
After the pre-treatment in the waste water each heavy metal concentration (mainly being free state) be respectively Cd=5.8mg/L, Zn, Pb, Cu concentration is lower than discharging standards, so do not consider. and Cd concentration still can not qualified discharge, so adopt gravity flow absorbing process of the present invention to handle.
3. upper prop absorption
Adsorption column is: parallel gravity flow multistage gradient adsorption column, the multistage adsorption column of the high 3cm of adsorption column of 3 polyphones is arranged in parallel, two adjacent column outlets link to each other with import, it is 1cm that the water-in water level of single absorbing unit is higher than water outlet water level waterhead, and the water sample that comes out from a last outlet can directly enter next inlet and carrying out adsorption treatment like this.With fully the suction sorbing material be filled in the adsorption column, flow rate control at 10ml/h until reaching processing requirements.
4. subsequent disposal
Handle the sorbent material behind the noble metal, recycle noble metal in the sewage with sour dissolution method when its sorbent material reaches capacity capacity.Can adopt simultaneously sludge dewatering, directly landfill, air-dry, burn and have the plant of super enrichment, rejection, tolerance to carry out biological restoration or biological fixation heavy metal.
5. interpretation of result
The Cd of the water outlet General Logistics Department detects with atomic absorption spectrophotometry, the result of detected result and embodiment 1 is similar, the concentration of Cd all is that less than its difference of 0.1mg/L. parallel processing mode can improve the treatment capacity in the unit time in the water outlet, compare with series connection, handling wastewater flow rate in the present embodiment unit time is 15mL/h, and the treatment capacity of tandem arrangement is 5mL/h.
1. sorbing material pre-treatment:
Sorbent material is: through the natural adsorbent behind the sulfonation modifying be: diatomite.Sorbent material is dried, be ground into 200 purpose particles then, with being immersed in the water, the back for the treatment of to absorb water fully is stand-by when using then.
2. the pre-treatment of treatment sewage
The preparation of simulated wastewater is identical with embodiment 1, with 5% and 1.0%HCl be adjusted to pH=4.0.
3. upper prop absorption
Adsorption column is: network type gravity flow multistage gradient adsorption column, link to each other by pipeline between the parallel adsorption column that is arranged in parallel, form a pair of three mode of communicating, promptly network-like, it is 1cm that the water-in water level of single absorbing unit is higher than water outlet water level waterhead, water sample after the adsorption column of upper level is handled is being handled by the adsorption column that pipeline flows into next stage, can not link to each other owing to there is waterhead between the adsorption column of parallel position, can only be that the outlet of upper level adsorption column links to each other with next stage or following next stage adsorption column.With fully the suction sorbing material be filled in the adsorption column, flow rate control at 15ml/h until reaching processing requirements.
4. subsequent disposal
Handle the sorbent material behind the noble metal, recycle noble metal in the sewage with sour dissolution method when its sorbent material reaches capacity capacity.Can adopt simultaneously sludge dewatering, directly landfill, air-dry, burn and have the plant of super enrichment, rejection, tolerance to carry out biological restoration or biological fixation heavy metal.
5. interpretation of result
The result of detected result and embodiment 1 is similar, and the concentration of Cd is all less than 0.1mg/L. in the water outlet
When adopting network type gravity flow multistage gradient adsorption column in the next stage adsorption column some or several adsorption columns reached loading capacity or broken down, can change current and stop route and replace temporarily, thereby not influence the operation conditions of whole technology.
Comparative example
With the adsorption column of traditional vertical-type arranged in series as (a) handling Cd as Fig. 1
2+The heavy metal wastewater thereby test conditions is identical with the preparation of embodiment 1 simulated sewage: contain Cd concentration in the simulation heavy metal water sample that uses in the test and be 56.0mgL
-1Contain peat 2.0g in the peat post, the about 5ml of peat column volume, the high 3cm of adsorption column, flow rate control 5mL/h, water outlet Cd detects (as Fig. 3) with atomic absorption spectrophotometry. and this shows and work as the water inlet water level promoting to certain altitude (6 meters), clear height as the vertical-type adsorption column is 3 meters, this traditional technology can only be settled 2 adsorption columns and gravity flow plural serial stage adsorption column difference of altitude of the present invention is 1 meter, can lay 6, and the sorbent material volume of laying in the single asymmetric u type pipe (quality) is suitable with single vertical-type adsorption column. that is to say, use identical energy (being used for promoting the water inlet water level), handle the water yield and improved 3 times, usefulness has improved 3 times. because the sorbing material volume that waste water is flowed through has improved 3 times, the water outlet effect more, it is bigger to handle the water yield.
Can find out that by data as Cd wastewater discharge standard＜0.1mg/L, the manageable water yield of technology of the presently claimed invention is higher than 1000ml as shown in Figure 4, and the wastewater flow rate that traditional adsorption column technology can only be handled reaches and is about 180ml.The treatment capacity of the gravity flow multistage gradient adsorption column among the present invention reaches 6 times that are about the latter.The advantage of embodiment 2 has been to improve the treatment capacity in the unit time simultaneously, and the advantage of embodiment 3 (network flow) is the fault that may occur when having avoided parallel connection or tandem process operation.So fundamentally improved the adsorption efficiency and the effluent characteristics of heavy metal wastewater thereby.
Claims (7)
1. a multipole gradient adsorption channel adsorption technology comprises sorbent material pre-treatment → industrial sewage pre-treatment → upper prop absorption → subsequent disposal, and it is characterized in that: sorbent material adopts natural low-cost sorbent in the sorbent material pre-treatment, and particle is the 1-200 order; Be 4-10 with its pH regulator during the industrial sewage pre-treatment, sewage is by removal suspended substance or particulate matter such as sand filtration, precipitations before the upper prop absorption; The adsorption column that adopts during upper prop absorption is the multistage gradient adsorption column that contains a plurality of absorbing units; Each absorbing unit is made up of U type adsorption column, and wherein: the water inlet water level of single absorbing unit is higher than the water outlet water level, and the volume of the sorbing material that the feed-water end of single absorbing unit is filled or height will be higher than water side sorbing material volume or height.
2. by the described multipole gradient adsorption channel adsorption technology of claim 1, it is characterized in that: described natural low-cost sorbent is: sweet peaceful, peat, chitin or chitosan, dead biology, sea grass or algae, xanthate, zeolite, diatomite, clay, mud coal soil, gelatine, humic acids or liver moss.
3. by the described multipole gradient adsorption channel adsorption technology of claim 1, it is characterized in that: described sewage is based on heavy metal wastewater thereby, and taking second place is dyeing waste water.
4. by the described multipole gradient adsorption channel adsorption technology of claim 1, it is characterized in that: the curved shape of the described U type adsorption column left side and the right pipe is asymmetric.
5. by the asymmetric U type of the described multistage gradient of claim 1 adsorption column novel process, it is characterized in that: water inlet will be higher than water outlet in the height of fill material, and the height difference of described fill material is that the amount of add-on in water inlet pipe of sorbent material in the U type adsorption column is higher than rising pipe.
6. by the described multipole gradient adsorption channel adsorption technology of claim 1, it is characterized in that: the water inlet pipe height of next processing unit will be lower than a last unitary rising pipe height in the described adsorption column.
7. by the described multipole gradient adsorption channel adsorption technology of claim 1, it is characterized in that: the adsorption column of described multistage gradient is that upper level processing unit and next stage processing unit mode of communicating can be for one to one or one-to-many, be that upper and lower level processing unit connects by network-like mode, utilize the multistage gradient of formation gravity flow of the self gravitation of waterhead and water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100456359A CN100447094C (en) | 2006-01-11 | 2006-01-11 | Multistage gradient adsorption channel adsorption technology |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100456359A CN100447094C (en) | 2006-01-11 | 2006-01-11 | Multistage gradient adsorption channel adsorption technology |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN100999344A true CN100999344A (en) | 2007-07-18 |
| CN100447094C CN100447094C (en) | 2008-12-31 |
Family
ID=38258183
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2006100456359A Expired - Fee Related CN100447094C (en) | 2006-01-11 | 2006-01-11 | Multistage gradient adsorption channel adsorption technology |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100447094C (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102327703A (en) * | 2011-07-28 | 2012-01-25 | 许盛英 | Method for dehydrating alcohol-based sterilizing and fresh-keeping solution |
| CN103172134A (en) * | 2013-03-05 | 2013-06-26 | 湖北大学 | Process and device used for removing heavy metal in biogas slurry |
| CN104944500A (en) * | 2015-05-26 | 2015-09-30 | 陕西工信环保科技发展有限公司 | Control method for continuously treating heavy-metal-containing liquid |
| CN106145220A (en) * | 2016-08-25 | 2016-11-23 | 贵州万山兴隆锰业有限公司 | A kind of manganese ore gives up material for water treatment and preparation method thereof |
| CN107129051A (en) * | 2017-06-23 | 2017-09-05 | 桂林理工大学 | A kind of method for improving artificial wetland treatment heavy metal wastewater thereby |
| CN112047516A (en) * | 2020-07-31 | 2020-12-08 | 张家港市大新污水处理有限公司 | Sewage filtering process without adding flocculating agent |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1405827A4 (en) * | 2001-05-21 | 2005-08-17 | Mitsubishi Electric Corp | Process and apparatus for treating nitrogen compound containing water |
| KR100443108B1 (en) * | 2002-03-25 | 2004-08-04 | 한상배 | Advanced Waste Water Treatment System with Intermittent Aeration, Biofilm and Bio Absorption |
| CN1195878C (en) * | 2003-03-12 | 2005-04-06 | 福建紫金矿业股份有限公司 | Gravity flow static adsorption method in gold ore bulk leaching |
-
2006
- 2006-01-11 CN CNB2006100456359A patent/CN100447094C/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102327703A (en) * | 2011-07-28 | 2012-01-25 | 许盛英 | Method for dehydrating alcohol-based sterilizing and fresh-keeping solution |
| CN102327703B (en) * | 2011-07-28 | 2013-08-14 | 许盛英 | Method for dehydrating alcohol-based sterilizing and fresh-keeping solution |
| CN103172134A (en) * | 2013-03-05 | 2013-06-26 | 湖北大学 | Process and device used for removing heavy metal in biogas slurry |
| CN104944500A (en) * | 2015-05-26 | 2015-09-30 | 陕西工信环保科技发展有限公司 | Control method for continuously treating heavy-metal-containing liquid |
| CN104944500B (en) * | 2015-05-26 | 2017-01-25 | 陕西工信环保科技发展有限公司 | Control method for continuously treating heavy-metal-containing liquid |
| CN106145220A (en) * | 2016-08-25 | 2016-11-23 | 贵州万山兴隆锰业有限公司 | A kind of manganese ore gives up material for water treatment and preparation method thereof |
| CN107129051A (en) * | 2017-06-23 | 2017-09-05 | 桂林理工大学 | A kind of method for improving artificial wetland treatment heavy metal wastewater thereby |
| CN112047516A (en) * | 2020-07-31 | 2020-12-08 | 张家港市大新污水处理有限公司 | Sewage filtering process without adding flocculating agent |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100447094C (en) | 2008-12-31 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102503030B (en) | System for treating heavy metal wastewater | |
| CN102951749B (en) | Method and device for removing heavy metals in industrial wastewater by nanoscale zero-valent iron-multilevel reversed filter type system | |
| CN100447094C (en) | Multistage gradient adsorption channel adsorption technology | |
| Ali et al. | Recent advances in technologies for removal and recovery of selenium from (waste) water: A systematic review | |
| CN204325024U (en) | A kind of novel lead-acid storage battery heavy metal waste water treatment system | |
| Zhang et al. | Research progress, problems and prospects of mine water treatment technology and resource utilization in China | |
| Acheampong et al. | Low-cost technologies for mining wastewater treatment | |
| CN100341794C (en) | Method of treating heavy metal industrial effluent with turf as adsorbent | |
| Fang et al. | Tandem type PRBs-like technology implanted with targeted functional materials for efficient resourceful treatment of heavy metal ions from mining wastewater | |
| CN102649608B (en) | Process method for treating mine acidic waste water | |
| CN202558715U (en) | Treatment and reuse device for electrolytic manganese industrial wastewater | |
| CN102992437A (en) | Device, structure and process for processing ammonia-nitrogen sewage by aeration zeolite fluidized bed | |
| WO2009121093A1 (en) | Waste water treatment | |
| CN101497032A (en) | Method for preparing biological sorbent and method of use thereof | |
| CN103043834A (en) | Rear earth smelting wastewater treatment process | |
| CN102701517A (en) | Method for jointly treating acid mine wastewater by using organic matter and carbonate rock | |
| CN105502736A (en) | Metallurgical wastewater treatment system | |
| CN102092869A (en) | Processing method of waste acid in acid producing system | |
| CN102241446B (en) | Mine wastewater treatment method and device | |
| CN111807630A (en) | High-efficient molybdenum-removing vertical subsurface flow constructed wetland purification device | |
| CN201942575U (en) | Industrial wastewater treatment device | |
| CN204246946U (en) | For the high-efficient treatment device of coal mine deep well water body | |
| CN113387527B (en) | Treatment method of bottom mud with heavy metal and organic compound pollution | |
| CN214990980U (en) | Rural black and odorous water body clean system based on magnetic coagulation | |
| CN203065322U (en) | Slurry separating tower |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20081231 Termination date: 20100211 |