CN1919747A - Closed circuit processing technique for chromium-containing wastewater - Google Patents
Closed circuit processing technique for chromium-containing wastewater Download PDFInfo
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- CN1919747A CN1919747A CN 200610113126 CN200610113126A CN1919747A CN 1919747 A CN1919747 A CN 1919747A CN 200610113126 CN200610113126 CN 200610113126 CN 200610113126 A CN200610113126 A CN 200610113126A CN 1919747 A CN1919747 A CN 1919747A
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Abstract
The invention discloses a sealed-path circulating processing technology of chrome wastewater, which is characterized by the following: adopting hollow fiber film contactor; flowing or reflowing chrome wastewater in the pipe and case of contactor separately; utilizing liquid film selective translation feature to separate and enrich Cr (VI); making Cr (VI) in the waste water transport to disposing liquid to remove Cr (VI).
Description
Technical field:
The present invention relates to a kind of novel chromate waste water treatment technology, belong to field of environment protection.
Background technology:
Plating, process hides and chromic salts industry all discharge a large amount of chromate waste waters every year.Wherein, China every year only the quantity discharged of waste electroplating liquor containing chromium just reach 4,000,000,000 m
3It is acid that chromate waste water is, and chromium ion is mainly with Cr
6+Compound C rO
4 2-, Cr
2O
7 2-Form exist.Cr (VI) toxicity is bigger, and skin, mucous membrane, the upper respiratory system of human body had stronger pungency and corrodibility, has effect carcinogenic and the modificator gene sudden change after being absorbed by the body, and causes diseases such as lung cancer, bronchogenic carcinoma easily.Chromate waste water severe contamination water source, soil, the havoc ecotope.Therefore the highest permission emission concentration of GB8978-1996 " integrated wastewater discharge standard " strict restriction Cr (VI) is 0.5mgL
-1The harmless treatment of chromate waste water is one of indispensable process procedure of above-mentioned related industries.
The main methods of chromate waste water is as follows at present:
1. chemical precipitation method: be one of chromate waste water treatment process that is most widely used at present.Its principle is to add FeSO in waste water
4, Na
2SO
3Or reducing substances such as iron powder, make Cr
6+Be reduced to Cr
3+, and then add NaOH or milk of lime makes Cr
3+Precipitate and separate.Its maximum shortcoming is that secondary pollution is serious, produces a large amount of mud.And, make water outlet saltiness height because this process need add a large amount of chemical agents, can't recycle waste water resource.
2. electrolytic reduction: its principle is that iron anode is separated out Fe under the direct current effect
2+, with Cr
6+Be reduced to Cr
3+In the time of between waste water ph rises to 7～10.5, generate Cr (OH)
3Precipitation.This method need consume a large amount of electric energy, steel, and running expense is higher, and produces mud, causes secondary pollution.For reducing power consumption, add a large amount of NaCl in the waste water of being everlasting, improve electric conductivity, but also increased the saltiness of water simultaneously, processed waste water can not recycle.
3. ion exchange method: this method is utilized the exchange between the same sex ion in the exchange ion of ion exchange resin and the solution, thereby realizes that Cr (VI) separates.Though ion exchange method has advantages such as resource recycling, non-secondary pollution, this technical matters complexity, one-time investment are big, and regeneration of resin, problem of oxidation solution still not yet in effect.
Above-mentioned various traditional treatment method is owing to be subjected to the restriction of know-why, exist secondary pollution, waste water can't reuse or processing cost cross high defective.The novel treatment technology of liquid-film method processing waste water containing chrome has appearred utilizing in recent years.
Document 1:E.J.Fuller, N.N.Li.Extraction of chromium and zinc from cooling tower blowdown by lquid membranes[J] .J.Membr.Sci..1984,18:251, adopting Aliquat 336 is carrier, nonyl-decyl alcohol is made membrane solvent, polyamine is made the emulsion liquid membrane system of tensio-active agent, removes Cr (VI) and zinc in the cooling tower sewage, and effect is obvious.But there are problems such as swelling, liquid-sheet disintegration in the emulsion liquid membrane process, easily causes the separating effect forfeiture, and follow-up demulsification technology complexity, is difficult to large-scale promotion.
Document 2:C.A.Kozlowski, W Walkowiak.Applicability of liquid membranes inchromium (VI) transport with amines as ion carriers[J] .J.Membr Sci.2005 (266): 143-150, adopt the board-like support membrane of polyethylene, with TOA is carrier, NaOH solution is reverse-extraction agent separation of C r (VI), and final Cr (VI) content reaches 1.5mgL
-1The problem of immobilized liquid membrane maximum is that film liquid runs off seriously, and work-ing life is short, can not satisfy separation requirement.
Therefore,, need a kind of novel chromate waste water closed circuit circulatory system of exploitation, promote the realization of chromate waste water green treatment process for response China builds a conservation-minded society, the principles and policies of friendly environment society.
Summary of the invention:
The present invention is in order to overcome the shortcoming of above-mentioned chromate waste water treatment process, provide a kind of more economically, the treatment process of environmental protection.Present method adopts hollow fiber membrane contactors, chromate waste water and treatment solution are also flowed or counter-current flow at tube side, the shell side of contactor respectively, utilize the characteristics of liquid film selective migration, the Cr (VI) in the waste water is constantly moved in treatment solution, reach the purpose of removing Cr (VI).This method not only can realize the removal of Cr (VI), and the solution of waste water after treatment and enrichment Cr (VI) is all recyclable.
The device that the present invention adopts as shown in Figure 1, its core is hollow fiber membrane contactors (1), contactor is made up of the hollow-fibre membrane and the housing of some amount, be tube side in the hollow fiber film tube, managing outward is shell side; (7), (8) are respectively the tube side interface; (5), (6) are respectively the shell side interface; (3) the treatment solution Preparation tank that stirs for band is connected with the pump housing (2) with the tube side interface (7) of membrane contactor respectively; (4) be the chromate waste water storage tank, be connected with the pump housing (2 ') with the shell side interface (6) of membrane contactor respectively.Contactor can be vertically, level or place with arbitrary special angle, to reach the optimum handling effect.
Described tubular fibre mould material is hydrophobic class, and as polyvinylidene difluoride (PVDF), polyethylene, polypropylene class etc., internal diameter is 0.5～3.0mm, and external diameter is 0.6～4.0mm, and porosity is 30%～80%, can choose on market.
The concrete processing step of the present invention is as follows:
A. prepare treatment solution
With carrier and mixing diluents preparation extraction agent, wherein the diluent volume mark is 50%～90% earlier; Extraction agent and reverse-extraction agent are together put into treatment solution Preparation tank (3) again and fully stirred and be mixed with treatment solution, wherein the volume fraction of extraction agent is 1%～10%;
Carrier can use neutral extraction agent such as tbp, perhaps organic amine extraction agent such as TOA, Aliquat-336, Alamine-336 etc.; Thinner is organic solvent commonly used such as kerosene, benzene, toluene etc.
Reverse-extraction agent is basic solution or reductibility salts solution, and basic solution can be selected NaOH, KOH, CaOH for use
2, LiOH, Na
2CO
3Deng, the reductibility salts solution can be selected Na for use
2SO
3, K
2SO
3Deng.
B, sepn process
With pump (2) treatment solution in the Preparation tank (3) is pumped into the membrane contactor tube side from interface (7), flow through behind the membrane contactor, flow out from interface (8), get back to Preparation tank (3), use pump (2 ') that waste water is pumped into the membrane contactor shell side from interface (5) simultaneously, flow through behind the membrane contactor, flow out from interface (6), get back to storage tank (4), so cyclical operation, Cr in chromate waste water (VI) content is lower than 0.5mg/L, reaches discharging standards; Two strands of materials counter-current flow in contactor in the aforesaid operations; Tube side, shell side volumetric flow rate were at 50: 1～1: 50, and more excellent volumetric flow rate scope is 10: 1～1: 20.
Also can make two bursts of material concurrent flows in contactor:, behind the membrane contactor of flowing through, flow out from interface (5) as waste water being squeezed into the membrane contactor shell side from interface (6) with pump (2 ').Perhaps use pump (2) that the treatment solution in the Preparation tank (3) is pumped into the membrane contactor tube side from interface (8), behind the membrane contactor of flowing through, flow out, get back to Preparation tank (3) from interface (7).
Can regularly take out treatment solution and the processed waste water of saturated Cr (VI) during cyclical operation, and constantly replenish fresh treatment solution, waste water, realize operate continuously.Also can or adopt large-scale membrane contactor, realize the processing of waste water one way by a plurality of membrane contactor series and parallels.
After treatment solution separates through clarification, extraction agent and reverse-extraction agent phase-splitting, Cr (VI) is in reverse-extraction agent, and after acidification, this chromium-containing solution can be used as the passivating solution of chrome-plating process.
In the entire treatment process, the carrier in the extraction agent has " ferryboat " effect, seldom consumes, and therefore, extraction agent not only consumption is little, can reuse, and has effectively avoided organic secondary pollution problem.
Know-why of the present invention is: by add organic extractant in tube side fluid, make and form one deck liquid film in the hollow fiber conduit, utilize the characteristics of liquid film selective migration, the Cr (VI) in the waste water is constantly transmitted in treatment solution, thereby reach the purpose of removing Cr (VI) in the waste water.According to the characteristic of the non-equilibrium mass transfer of liquid film, utilize its " upward slope effect ", Cr (VI) can realize contrary concentration gradient migration: liquid film one side, the Cr in the waste water (VI) content continue to descend, and ultimate density is less than 0.5mg/L; Opposite side, Cr in the reverse-extraction agent (VI) content continue to rise, and ultimate density can be up to 2500mg/L.
Advantage of the present invention is: (1) hollow-fibre membrane provides huge mass transfer area, and resistance to mass transfer is little, so wastewater treatment speed is fast.(2) technical process is simple, and turndown ratio is big, and the fluid of hollow-fibre membrane both sides can independent regulation.(3) facility compact, volume is little, and is easy to amplify, and required function unit and interconnecting piece are few, and postprocessing working procedures is simple, so investment cost and process cost all can reduce significantly.(4) non-secondary pollution, obvious environment benefit.(5) waste water after treatment, the rinsing liquid that water resources can be used as plating piece reclaim to use, and reclaims the passivating solution that liquid can be used as electroplating process after treatment and reuses.
Description of drawings
Fig. 1 is novel chromate waste water treatment technology device synoptic diagram, wherein each sequence number representative: (1) hollow fiber membrane contactors; (2) reaching (2 ') is infusion pump; (3) treatment solution Preparation tank; (4) chromate waste water storage tank; (5) shell side interface; (6) shell side interface; (7) tube side interface; (8) tube side interface
Fig. 2 is Cr (VI) content and the graph of a relation in treatment time in embodiment 1 waste water
Fig. 3 is Cr (VI) content and the graph of a relation in treatment time in embodiment 2 treatment solutions
Fig. 4 is Cr (VI) content and the graph of a relation in treatment time in embodiment 3 waste water and the treatment solution
Embodiment
Adopt device shown in Figure 1, wherein used contactor useful length is 300mm, internal diameter 9.9mm; Hollow-fibre membrane is polyvinylidene difluoride (PVDF) (PVDF) material, and inside and outside footpath is respectively 0.812mm, 0.886, and loading level is 25.
A. be carrier with the tbp, be mixing diluents preparation extraction agent with kerosene, wherein the volume fraction of thinner is 60%; The NaOH that with concentration is 1mol/L is a reverse-extraction agent, is 5% quantitatively extraction agent and reverse-extraction agent two are added to treatment solution Preparation tank (3) and stir by the volume fraction of extraction agent in the treatment solution.
B. use pump (2) that the treatment solution in the Preparation tank (3) is contacted in the organ pipe from tube side interface (7) input, the ingress flow is 40ml/min, and treatment solution flows out from tube side interface (8) and comes back to Preparation tank (3).K with about 100mg/L
2Cr
2O
7The solutions simulate chromate waste water, regulating waste water acidity with HCl solution is that pH=0～1 back adds storage tank (4), with pump (2) chromate waste water in the storage tank (4) is imported the contactor shell side from shell side interface (5), flow is 40ml/min.Tube side, shell side throughput ratio are 1: 1, finish mass transfer after, flow out from shell side interface (6), enter storage tank again.So the chromium content of cyclical operation in waste water reaches emission standard.
Analyze water Cr (VI) concentration with diphenyl carbazide spectrophotometry.Cr in the chromate waste water (VI) content with the variation relation of handling the time as shown in Figure 2.As seen from Figure 2, behind about 90min of treatment time, Cr in the waste water (VI) concentration reaches discharging standards less than 0.5mg/L, and the average mass transfer flux of entire treatment process is 3600mg/m
2H.
Other operational conditions are identical with embodiment 1, and contactor length is 20cm, internal diameter 10.3mm, and hollow-fibre membrane filling radical is 20.The volume fraction of extraction agent is 2% in the treatment solution.Shell side chromate waste water flow is risen to 100ml/L, and the volume flow ratio of tube side and shell-side fluid is 1: 2.5.Strengthen the amount of pending waste water, the treatment solution consumption only is 1/30 of a wastewater flow rate.Cr in the treatment solution (VI) content with the variation relation of handling the time as shown in Figure 3.As seen from Figure 3, the final content of Cr (VI) can reach more than the 2500mg/L in the treatment solution.
Other operational conditions are identical with embodiment 1, change the tube side flow among the embodiment 1 into 20ml/min, and the shell side flow changes 50ml/min into; The volume fraction of thinner is 50% in the extraction agent.Variation relation is as shown in Figure 4 in time for Cr in chromate waste water and the treatment solution (VI) content.As seen from Figure 4, Cr in the treatment solution (VI) concentration can rise to about 80mg/L from 0, and simultaneously, Cr in the waste water (VI) density loss is to 0.5mg/L.
Adopt the uniprocessing method, promptly waste water flows out from shell side interface (6), does not enter storage tank (4).The tube side flow is 56ml/min, and the shell side flow is 1.5ml/min, and the volume flow ratio of tube side and shell-side fluid is 37.3: 1.The volume fraction of thinner is 50% in the extraction agent, other conditions such as embodiment 1.Measure shell side import and export Cr (VI) concentration, reduce to 35.0mg/L by 78.8mg/L, single-stage place to go rate reaches 55%, and the mass transfer flux is up to 11300mg/ (m
2H).Concrete data see Table 1.
The uniprocessing data of table 1 chromate waste water
| Project | Data |
| Inlet Cr (VI) concentration/place to go rate of mg/L outlet Cr (VI) concentration/mg/L/% duration of contact/min mass transfer area/m 2Mass transfer flux/mg/ (m 2·h) | 78.8 35.0 55 12.2 0.019 11300 |
Claims (6)
1. chromate waste water closed circulation processing technique, used device synoptic diagram as shown in Figure 1, its core component is hollow fiber membrane contactors (1), contactor is made up of hollow-fibre membrane and housing, hollow-fibre membrane is contained in the housing, in the hollow fiber film tube is tube side, pipe is outer to be shell side, (7), (8) be respectively the tube side interface, (5), (6) be respectively the shell side interface, (3) the treatment solution Preparation tank that stirs for band, be connected with the pump housing (2) with the tube side interface (7) of membrane contactor respectively, (4) be the waste water storage tank, be connected with the pump housing (2 ') with the shell side interface (6) of membrane contactor respectively, it is characterized in that adopting following processing step that chromate waste water is handled:
A, preparation treatment solution
With carrier and mixing diluents preparation extraction agent, wherein the diluent volume mark is 50%～90% earlier; Extraction agent and reverse-extraction agent are together put into treatment solution Preparation tank (3) again and fully stirred and be mixed with treatment solution, wherein the volume fraction of extraction agent is 1%～10%; Used carrier is neutral extraction agent or organic amine extraction agent, and thinner is the organic solvent of using always, and reverse-extraction agent is basic solution or reductibility salts solution;
B, sepn process
With pump (2) treatment solution in the Preparation tank (3) is pumped into the membrane contactor tube side from interface (7), flow through behind the membrane contactor, flow out from interface (8), get back to Preparation tank (3), use pump (2 ') that waste water is pumped into the membrane contactor shell side from interface (5) simultaneously, behind the membrane contactor of flowing through, flow out from interface (6), get back to storage tank (4), so cyclical operation, Cr in chromate waste water (VI) content reaches discharging standards; Tube side, shell side volume flow ratio between 50: 1～1: 50, two strands of materials counter-current flow in contactor in this process.
2. chromate waste water closed circulation processing technique according to claim 1, the treatment solution and the processed waste water of regularly taking out saturated Cr (VI) when it is characterized in that cyclical operation, and constantly replenish fresh treatment solution, waste water, realize operate continuously.
3. chromate waste water closed circulation processing technique according to claim 1 is characterized in that described carrier is a kind of among tbp, TOA, Aliquat-336, the Alamine-336; Thinner is a kind of in kerosene, benzene, the toluene; Basic solution is NaOH, KOH, CaOH
2, LiOH, Na
2CO
3In a kind of, the reductibility salts solution is Na
2SO
3Or K
2SO
3In a kind of.
4. chromate waste water closed circulation processing technique according to claim 1, the volume flow ratio that it is characterized in that the described tube side of step B, shell side is 10: 1～1: 20.
5. chromate waste water closed circulation processing technique according to claim 1 is characterized in that changing treatment solution or the flow direction of pending chromate waste water in contactor, makes two strands of materials do concurrent flow.
6. chromate waste water closed circulation processing technique according to claim 1 is characterized in that by a plurality of membrane contactor series and parallels or large-scale membrane contactor, realizes the processing of waste water one way.
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|---|---|---|---|
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| CN100393641C CN100393641C (en) | 2008-06-11 |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101829436A (en) * | 2010-05-27 | 2010-09-15 | 南京工业大学 | Large liquid film continuous reaction device |
| CN102154548A (en) * | 2011-03-18 | 2011-08-17 | 中国科学院地理科学与资源研究所 | Device and method for migration by adopting carrier mixed dual-phase sheet type combined liquid film |
| CN103551061A (en) * | 2013-11-15 | 2014-02-05 | 天津工业大学 | Preparation method of high-negative charge density hollow fiber nanofiltration membrane for removing Cr(VI) from water |
| CN105344130A (en) * | 2015-12-07 | 2016-02-24 | 上海绿强新材料有限公司 | Method for removing heavy metal in traditional Chinese medicine by means of zeolite molecular sieve membrane |
| CN108975621A (en) * | 2018-08-13 | 2018-12-11 | 漳州香洲皮革有限公司 | A kind of the sewage classification processing system and processing method of leather production |
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| CN103304005A (en) * | 2012-03-15 | 2013-09-18 | 北京化工大学 | Method for removing phenol in phenol contained wastewater by using hollow fiber membrane |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2179650B1 (en) * | 1972-04-14 | 1974-07-26 | Ugine Kuhlmann | |
| CN1106361A (en) * | 1994-02-02 | 1995-08-09 | 东北师范大学 | Treatment method of chromium-containing wastewater |
| CN100363092C (en) * | 2005-10-14 | 2008-01-23 | 中冶焦耐工程技术有限公司 | Ultrafiltration membrane for treating coking sewage |
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2006
- 2006-09-15 CN CNB2006101131265A patent/CN100393641C/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101829436A (en) * | 2010-05-27 | 2010-09-15 | 南京工业大学 | Large liquid film continuous reaction device |
| CN101829436B (en) * | 2010-05-27 | 2012-06-27 | 南京工业大学 | Large liquid film continuous reaction device |
| CN102154548A (en) * | 2011-03-18 | 2011-08-17 | 中国科学院地理科学与资源研究所 | Device and method for migration by adopting carrier mixed dual-phase sheet type combined liquid film |
| CN103551061A (en) * | 2013-11-15 | 2014-02-05 | 天津工业大学 | Preparation method of high-negative charge density hollow fiber nanofiltration membrane for removing Cr(VI) from water |
| CN105344130A (en) * | 2015-12-07 | 2016-02-24 | 上海绿强新材料有限公司 | Method for removing heavy metal in traditional Chinese medicine by means of zeolite molecular sieve membrane |
| CN105344130B (en) * | 2015-12-07 | 2017-07-14 | 上海绿强新材料有限公司 | A kind of method of heavy metal in utilization zeolite molecular sieve film removing Chinese medicine |
| CN108975621A (en) * | 2018-08-13 | 2018-12-11 | 漳州香洲皮革有限公司 | A kind of the sewage classification processing system and processing method of leather production |
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