CN101462801A - System and process for desalting steel comprehensive sewage reuse water by double-membrane method - Google Patents
System and process for desalting steel comprehensive sewage reuse water by double-membrane method Download PDFInfo
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- 238000000034 method Methods 0.000 title claims abstract description 33
- 229910000831 Steel Inorganic materials 0.000 title claims abstract description 26
- 239000010959 steel Substances 0.000 title claims abstract description 26
- 238000011033 desalting Methods 0.000 title claims abstract description 17
- 239000012528 membrane Substances 0.000 title claims abstract description 14
- 239000010865 sewage Substances 0.000 title abstract description 23
- 230000008569 process Effects 0.000 title abstract description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 50
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 49
- 238000001914 filtration Methods 0.000 claims abstract description 31
- 229910052742 iron Inorganic materials 0.000 claims abstract description 25
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 24
- 238000010612 desalination reaction Methods 0.000 claims abstract description 23
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 19
- 238000001816 cooling Methods 0.000 claims abstract description 13
- 238000005189 flocculation Methods 0.000 claims abstract description 7
- 230000003647 oxidation Effects 0.000 claims abstract description 7
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 7
- 239000002351 wastewater Substances 0.000 claims description 21
- 239000002131 composite material Substances 0.000 claims description 20
- 230000003311 flocculating effect Effects 0.000 claims description 20
- 239000002480 mineral oil Substances 0.000 claims description 12
- 235000010446 mineral oil Nutrition 0.000 claims description 12
- 238000005516 engineering process Methods 0.000 claims description 10
- 239000000126 substance Substances 0.000 claims description 10
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 claims description 9
- 239000000084 colloidal system Substances 0.000 claims description 9
- 229910052748 manganese Inorganic materials 0.000 claims description 9
- 239000011572 manganese Substances 0.000 claims description 9
- 238000005115 demineralization Methods 0.000 claims description 8
- 239000003795 chemical substances by application Substances 0.000 claims description 7
- 230000002328 demineralizing effect Effects 0.000 claims description 7
- 238000002203 pretreatment Methods 0.000 claims description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 5
- 229910052799 carbon Inorganic materials 0.000 claims description 5
- 239000000706 filtrate Substances 0.000 claims description 5
- 230000016615 flocculation Effects 0.000 claims description 5
- 229910001385 heavy metal Inorganic materials 0.000 claims description 5
- 238000005273 aeration Methods 0.000 claims description 4
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 claims description 4
- 150000002500 ions Chemical class 0.000 claims description 4
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 claims description 4
- 239000006004 Quartz sand Substances 0.000 claims description 3
- 229910021578 Iron(III) chloride Inorganic materials 0.000 claims description 2
- RUTXIHLAWFEWGM-UHFFFAOYSA-H iron(3+) sulfate Chemical compound [Fe+3].[Fe+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O RUTXIHLAWFEWGM-UHFFFAOYSA-H 0.000 claims description 2
- 229910000360 iron(III) sulfate Inorganic materials 0.000 claims description 2
- 239000004576 sand Substances 0.000 claims description 2
- 238000004064 recycling Methods 0.000 abstract description 3
- 238000004140 cleaning Methods 0.000 abstract description 2
- 238000009298 carbon filtering Methods 0.000 abstract 1
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 9
- 230000000694 effects Effects 0.000 description 7
- 239000004912 1,5-cyclooctadiene Substances 0.000 description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- 239000003814 drug Substances 0.000 description 4
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 4
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- 238000002347 injection Methods 0.000 description 2
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- 239000004571 lime Substances 0.000 description 2
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 2
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- 241000894006 Bacteria Species 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- DWAQJAXMDSEUJJ-UHFFFAOYSA-M Sodium bisulfite Chemical compound [Na+].OS([O-])=O DWAQJAXMDSEUJJ-UHFFFAOYSA-M 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
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- 125000001309 chloro group Chemical group Cl* 0.000 description 1
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- 239000012466 permeate Substances 0.000 description 1
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- 238000005096 rolling process Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 235000010267 sodium hydrogen sulphite Nutrition 0.000 description 1
- 238000009628 steelmaking Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 230000003245 working effect Effects 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
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- Water Treatment By Sorption (AREA)
Abstract
A system and a process for desalting steel comprehensive sewage reuse water by a double-membrane method, belonging to the technical field of sewage treatment and reuse. The system comprises a cooling tower, a raw water tank, a micro-flocculation filtering device, a bypass flow activated carbon filtering tank, a laminated filter, an ultrafiltration system, a precision filter, a reverse osmosis system and a reverse osmosis desalting water tank. Is used for solving the problem of desalting of the comprehensive sewage reuse water of the iron and steel enterprises by a double-membrane method. Desalting by adopting a double-membrane method, treating pretreated water by an ultrafiltration device to meet the requirement that SDI is less than or equal to 3, and desalting by a reverse osmosis device. The method treats the recycled water of the steel and iron comprehensive sewage in a mode combining pre-oxidation, micro-flocculation filtration, bypass flow activated carbon filtration and self-cleaning filtration, greatly improves the operation stability and the service life of the double-membrane desalination system, effectively realizes sewage recycling and sewage zero discharge, and has important practical value for desalination of the recycled water of the steel and iron comprehensive sewage.
Description
Technical field
The invention belongs to steel iron wastewater and handle and the reuse technology field, particularly a kind of system of steel composite wastewater recycle-water double-membrane demineralization and technology are applicable to the advanced treatment and the desalination reuse of iron and steel composite wastewater.
Background technology
Reusing sewage is that iron and steel enterprise realizes an important channel of " water-saving and emission-reducing ".Be water saving, improve the repeating utilization factor of whole Steel Plant water resources, drop into sewage work in succession as water rich and influential family's Iron And Steel Company, the water after will handling through sewage work carry out reuse, to save the magnitude of recruitment of source water; Simultaneously, because factors such as whole Steel Plant water system concentrates, evaporation, enter the sewage quality complexity of sewage work, saltiness is higher, the reusing sewage that does not have advanced desalination to handle, the corrosion tendency that cause the saltiness of Steel Plant's water system to raise, cycles of concentration improves difficult and aggravation system etc.
At present, domestic Iron And Steel Company be mostly to composite wastewater (containing the factory effluent that is no more than 30% sanitary sewage) adopt lime softening-clarification-filtration-sterilization process carries out pair embrane method desalination reuses after reaching the reuse water requirement.Because sewage work's quality of reused water is complicated and fluctuation is bigger, two embrane method desalting system life-spans are very short, and operation is very unstable.So, some company has increased some pre-treatment measures before two embrane method desalting systems, as increase the cooling tower cooling in summer, increase little flocculation and remove part suspended substance, colloid and COD, increase laminated filter and remove the part suspended substance, the injection Powdered Activated Carbon is removed and is partly dissolved organic matter before raw water box, or even the combination of these measures.Obviously, these measures all can only improve the water quality that enters two embrane method desalting systems from some aspect; Though some measure can solve some problems, but produced new problem, as adopting injection powder process of active carbon, though the content of economic reduction dissolved organic matter comparatively easily makes follow-up laminated filter and UF stop up.
Above-mentioned situation causes the two embrane method desalting systems of existing composite wastewater reuse water that following subject matter is arranged: it is dirty stifled that 1. ultrafiltration system is subject to colloid, causes transmembrane pressure to raise, and membrane flux reduces, and cleaning frequency obviously increases; 2. reverse osmosis system is subject to the heavy-metal pollution such as iron, manganese in the sewage, or at some dead angles owing to microorganism is grown in organic existence.3. stifled operating pressure rising, the increasing of medicine consumption, the power consumption of two embrane method desalting systems of all making of various dirts increases.In view of the above problems, should update the steel composite wastewater recycle-water double-membrane demineralization technology, its key problem is to strengthen two pretreated abilities of embrane method desalination.
Summary of the invention
The system and the technology that the objective of the invention is to overcome the deficiencies in the prior art and a kind of steel composite wastewater recycle-water double-membrane demineralization is provided realize sewage recycling and Steel Plant's sewage " zero release ".
System of the present invention comprises cooling tower 1, raw water box 2, raw water pump 3, micro flocculating filter device 4, by-pass flow water pump 5, by-pass flow activated carbon filtration jar 6, water pump 7, laminated filter 8, ultrafiltration system 9, accurate filter 10, reverse osmosis system 11.Wherein, cooling tower 1, raw water box 2, raw water pump 3, micro flocculating filter device 4, by-pass flow water pump 5, by-pass flow activated carbon filtration jar 6, water pump 7, laminated filter 8 form two embrane method desalination pretreatment systems by pipe connection successively, and ultrafiltration system 9, accurate filter 10, reverse osmosis system 11, reverse osmosis desalination water tank 12 form two embrane method desalting systems by pipe connection successively.
Micro flocculating filter device of the present invention links to each other with laminated filter with water pump successively by pipeline, on the pipeline between micro flocculating filter device and the water pump, by-pass flow water pump and by-pass flow activated carbon filtration jar are set, and by-pass flow water pump and by-pass flow activated carbon filtration jar pass through pipe connection.
The filtering accuracy of laminated filter of the present invention is got 20～200 μ m; The filtering accuracy of described accurate filter is got 5～20 μ m.
Technology of the present invention is undertaken by following operation:
1. two embrane method desalination pre-treatment: the iron and steel composite wastewater is reached suspended substance after treatment less than 25mg/L, COD
CrLess than 40mg/L, mineral oil less than 3mg/L, temporary hardness less than the reuse water of 100mg/L successively after overcooling, preoxidation, micro flocculating filter, by-pass flow activated carbon filtration and laminated filter are handled, remove most of heavy metal ion, colloid, organism and mineral oil, make its suspended substance less than 5mg/L, COD
CrLess than 10mg/L, mineral oil less than 0.5mg/L, iron less than 0.5mg/L, manganese less than 0.5mg/L.
2. two embrane method desalinations: will handle through ultra-filtration equipment earlier through pretreated water, and reach the requirement of SDI≤3, and carry out the desalination processing through entering reverse osmosis unit behind the accurate filter again.
Preoxidation of the present invention is to utilize the water collecting basin of cooling tower or raw water box to carry out preoxidation, and preoxidation can be adopted the way of aeration or dosing oxidation, to promote the oxidation of iron, manganese.
The filtrate of micro flocculating filter device of the present invention adopts quartz sand or manganese sand, and (hydraulic detention time, english abbreviation are HRT to hydraulic detention time, and popular saying is exactly " duration of contact " or " action time ".) HRT=5～30min, design filtering velocity 8～20m/h.
The flocculation agent of micro flocculating filter device of the present invention is selected FeCl for use
3(iron trichloride), PFC (poly-ferric chloride) or PFS (bodied ferric sulfate), dosage is 2～15mg/L, or adds PAC (polymerize aluminum chloride), dosage is 1～15mg/L.
It is filtrate that by-pass flow activated carbon filtration jar of the present invention adopts granulated active carbon, adopts the fixed bed mode, and the by-pass flow water yield is 0.1～100% of a Total Water, and concrete ratio needs to set hydraulic detention time HRT=1～15min according to quality of reused water.
The present invention has the technological improvement of 2 innovations: the one, improve the removal ability of iron, manganese, and adopt and carry out preoxidation at the water collecting basin of cooling tower or raw water box and realize this effect; The 2nd, micro flocculating filter-activated carbon filtration combination process has the Synergistic degradation effect to turbidity, colloid, the organism of sewage, and adopts granulated active carbon to be difficult for stopping up follow up device, laminated filter is set can guarantees that more ultrafiltration system is not blocked.
Advantage of the present invention and positively effect are:
Filter combined mode iron and steel composite wastewater reuse water is handled with preoxidation, micro flocculating filter, by-pass flow activated carbon filtration, self-stip, under the situation that only needs to increase a small amount of investment and take up an area of, improved the stable and work-ing life of two embrane method desalting systems greatly, greatly reduce medicine consumption and power consumption, effectively realized sewage recycling and sewage " zero release ", the better economic effect has been arranged.
2. micro flocculating filter-activated carbon filtration combination process has the Synergistic degradation effect to turbidity, colloid, the organism of sewage, increases preoxidation and can further strengthen iron, manganese, organic Degradation before micro flocculating filter.The present invention has important practical to be worth to steel composite wastewater recycle-water double-membrane demineralization.
Description of drawings
Fig. 1 is a steel composite wastewater recycle-water double-membrane demineralization system diagram of the present invention.Wherein, cooling tower 1, raw water box 2, raw water pump 3, micro flocculating filter device 4, by-pass flow water pump 5, by-pass flow activated carbon filtration jar 6, water pump 7, laminated filter 8, ultrafiltration system 9, accurate filter 10, reverse osmosis system 11, reverse osmosis desalination water tank 12, preoxidation with pressurized air or oxidation medicament 13, little flocculation with flocculation agent 14, sterilant 15, transfer pH with hydrochloric acid 16, Scale inhibitors 17, reductive agent 18, accent pH with sodium hydroxide 19, iron and steel composite wastewater reuse water 20, de-mineralized water confess 21, the dense water 22 of ultrafiltration, reverse osmosis concentrated water 23.
Embodiment
The present invention will be further described below in conjunction with accompanying drawing.
The present invention is applicable to the advanced treatment and the desalination reuse of iron and steel composite wastewater.
1. two embrane method desalination pre-treatment: the iron and steel composite wastewater is reached suspended substance after treatment less than 25mg/L, COD
CrHandle through overcooling, preoxidation, micro flocculating filter, by-pass flow activated carbon filtration and laminated filter successively less than the reuse water of 100mg/L less than 3mg/L, temporary hardness less than 40mg/L, mineral oil.The present invention through Technological Economy relatively determines to adopt water collecting basin or raw water box at cooling tower to carry out aeration preoxidation, than adding medicament oxidation economy, and follow-up pair of embrane method desalting system not have to damage substantially.For by-pass flow activated carbon filtration jar; adopt granulated active carbon to be difficult for stopping up follow up device; laminated filter is set guarantees that more ultrafiltration system is not blocked; adopt the fixed bed mode; the by-pass flow water yield is 0.1～100% of a Total Water; concrete ratio can be regulated hydraulic detention time HRT=1～15min according to quality of reused water.
The composite wastewater reuse water can be removed most of heavy metal ion, colloid, organism and mineral oil through after the pre-treatment, makes its suspended substance less than 5mg/L, COD
CrLess than 10mg/L, mineral oil less than 0.5mg/L, iron less than 0.5mg/L, manganese less than 0.5mg/L.
2. two embrane method desalting systems: will handle through ultra-filtration equipment earlier through pretreated water, and remove colloid silicon, biological pollutant, particulate matter, turbidity, bacterium in the water, and reach the requirement of SDI≤3, and satisfy the requirement that enters reverse osmosis, and enter ultrafiltration and produce water tank.Pass through accurate filter again, the tapered structure of its filter opening, filtration can enter the depths, forms Depth Filtration, and pollutant holding capability is big, and the life-span is long, is convenient to quick replacing, and follow-up reverse osmosis unit is played good security personnel's effect.Enter reverse osmosis unit afterwards and carry out the desalination processing, the reverse osmosis unit major function is the salinity that removes in the water, and ratio of desalinization is greater than 96%.
Specific embodiment below is provided:
1. the pre-treatment of two embrane method desalination: the iron and steel composite wastewater that certain Iron And Steel Company mixes smelting, rolling effluent and all the other about sanitary sewages of about 24% through coarse rack-fine fack-lime softening-after high dense settling pond-pH regulator-V-type filter tank-add NaClO disinfects, produce into suspended substance less than 20mg/L, COD
CrLess than 30mg/L, mineral oil less than 3mg/L, temporary hardness reuse water less than 100mg/L, chlorine residue 0.5mg/L, more successively through the overcooling control water temperature at 8～30 ℃, the preoxidation of cooling tower water collecting basin aeration, former pond, raw water pump, to select quartz sand for use be filtrate and the FeCl that adds 3～10mg/L
3(iron trichloride) carries out 10～50% of micro flocculating filter, setting Total Water and carries out the by-pass flow activated carbon filtration, is the laminated filter processing of 55 μ m again through filtering accuracy.In addition, for suppressing bacterial reproduction in the water, behind raw water pump, need add sterilant and carry out germicidal treatment, sterilant can adopt NaClO (clorox), and adding dose is 0.5～3mg/L, in order to guarantee the sterilization effect of NaClO, also need regulate pH 5.5～7.0, can add a certain amount of hydrochloric acid.The composite wastewater reuse water can be removed most of heavy metal ion, colloid, organism and mineral oil through after the pre-treatment, guarantees that suspended substance is less than 5mg/L, COD
CrLess than 10mg/L, mineral oil less than 0.5mg/L, iron less than 0.1mg/L, manganese less than 0.05mg/L.
2. two embrane method desalting systems: will handle through the inner pressed ultra-filtration equipment earlier through pretreated water, and reach the requirement of SDI≤2, and send into ultrafiltration and produce water tank, the dense water of ultrafiltration then drains into network of drains.Be to enter reverse osmosis unit after boosting with high-pressure pump behind the accurate filter of 5 μ m to carry out desalination and handle through precision again.Water is produced in ultrafiltration need add reductive agent and Scale inhibitors and the mixing of process line mixer before entering accurate filter, wherein Scale inhibitors can be PTP0100 efficient scale/dispersion agent that the U.S. clear power company produces, and adding dosage is 3～5mg/L; Reductive agent adopts NaHSO
3(sodium bisulfite), dosing dosage are 1～3mg/L, guarantee to enter the preceding cl content of reverse osmosis unit less than 0.1mg/L.The concentrated water drainage of reverse osmosis is gone out stewing slag, the reverse osmosis permeate water adds NaOH (sodium hydroxide) and regulates about pH to 7.0, send sweet-water tank to through the line mixer mixing, use as the steel-making sheet billet continuous casting, also can be used as make up water or other water of productive use of circulating water system for the associated user.
Claims (7)
1, a kind of system of steel composite wastewater recycle-water double-membrane demineralization, its feature exists
, this system comprises cooling tower (1), raw water box (2), raw water pump (3), micro flocculating filter device (4), by-pass flow water pump (5), by-pass flow activated carbon filtration jar (6), water pump (7), laminated filter (8), ultrafiltration system (9), accurate filter (10), reverse osmosis system (11), reverse osmosis desalination water tank (12); Wherein, cooling tower, raw water box, raw water pump, micro flocculating filter device, by-pass flow water pump, by-pass flow activated carbon filtration jar, water pump, laminated filter form two embrane method desalination pretreatment systems by pipe connection successively, and ultrafiltration system, accurate filter, reverse osmosis system, reverse osmosis desalination water tank form two embrane method desalting systems by pipe connection successively.
2, system according to claim 1, it is characterized in that, described micro flocculating filter device links to each other with laminated filter with water pump successively by pipeline, on the pipeline between micro flocculating filter device and the water pump, by-pass flow water pump and by-pass flow activated carbon filtration jar are set, and by-pass flow water pump and by-pass flow activated carbon filtration jar pass through pipe connection.
3, system according to claim 1 is characterized in that, the filtering accuracy of described laminated filter is got 50～200 μ m; The filtering accuracy of described accurate filter is got 5～20 μ m.
4, the described system of a kind of employing claim 1 steel composite wastewater recycle-water double-membrane demineralization method is characterized in that,
(1) two embrane method desalination pre-treatment: the iron and steel composite wastewater is reached suspended substance after treatment less than 25mg/L, COD
CrLess than 40mg/L, mineral oil less than 3mg/L, temporary hardness less than the reuse water of 100mg/L successively after overcooling, preoxidation, micro flocculating filter, by-pass flow activated carbon filtration and laminated filter are handled, remove most of heavy metal ion, colloid, organism and mineral oil, make its suspended substance less than 5mg/L, COD
CrLess than 10mg/L, mineral oil less than 0.5mg/L, iron less than 0.5mg/L, manganese less than 0.5mg/L;
(2: two embrane method desalinations: will handle through ultra-filtration equipment earlier through pretreated water, and reach the requirement of SDI≤3, and carry out the desalination processing through entering reverse osmosis unit behind the accurate filter again.
5, technology according to claim 4 is characterized in that, utilizes the water collecting basin of cooling tower or raw water box to carry out preoxidation, and the way of aeration or dosing oxidation is adopted in preoxidation, to promote the oxidation of iron, manganese.
6, technology according to claim 4 is characterized in that, the filtrate of described micro flocculating filter adopts quartz sand or manganese sand, hydraulic detention time HRT=5～30min, design filtering velocity 8～20m/h; Flocculation agent is selected FeCl for use
3, poly-ferric chloride or bodied ferric sulfate, dosage is 2～15mg/L, or adds polymerize aluminum chloride, dosage is 1～15mg/L.
7, technology according to claim 4 is characterized in that, it is filtrate that described by-pass flow activated carbon filtration adopts granulated active carbon, hydraulic detention time HRT=1～15min.
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| CN2009100770250A CN101462801B (en) | 2009-01-16 | 2009-01-16 | System and process for desalting steel comprehensive sewage reuse water by double-membrane method |
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Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102030437A (en) * | 2010-11-04 | 2011-04-27 | 河北省首钢迁安钢铁有限责任公司 | Method for comprehensive wastewater desalination and zero release in steel production |
| CN102161539A (en) * | 2010-06-23 | 2011-08-24 | 隆润新技术发展有限公司 | Application of combined technology of high-density filtering pond and V-shaped filtering pond in deep processing method of coking wastewater |
| CN102206020A (en) * | 2011-05-03 | 2011-10-05 | 中冶赛迪工程技术股份有限公司 | Zero-emission comprehensive treatment process and system for waste water from whole plant of steelmaking enterprise |
| CN103408193A (en) * | 2013-08-16 | 2013-11-27 | 北京首钢国际工程技术有限公司 | Process for preparing desalted water for iron and steel plants with slightly polluted surface water as water source |
| CN104176845A (en) * | 2013-05-20 | 2014-12-03 | 宝山钢铁股份有限公司 | Cold-rolling alkaline oil-containing wastewater reuse treatment method |
| CN104671499A (en) * | 2015-02-01 | 2015-06-03 | 山西太钢不锈钢股份有限公司 | Advanced treatment and quality-divided recycling method of comprehensive smelting sewage |
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Address after: 100000 Shijingshan Road, Shijingshan District, Shijingshan District, Beijing Co-patentee after: Shougang Jingtang United Iron & Steel Co., Ltd. Patentee after: SHOUGANG GROUP Co.,Ltd. Co-patentee after: BEIJING SHOUGANG INTERNATIONAL ENGINEERING TECHNOLOGY Co.,Ltd. Address before: 100000 Shijingshan Road, Shijingshan District, Shijingshan District, Beijing Co-patentee before: Shougang Jingtang United Iron & Steel Co., Ltd. Patentee before: SHOUGANG Corp. Co-patentee before: BEIJING SHOUGANG INTERNATIONAL ENGINEERING TECHNOLOGY Co.,Ltd. |