CN111592155A - Intelligent integrated emergency water treatment equipment and method - Google Patents
Intelligent integrated emergency water treatment equipment and method Download PDFInfo
- Publication number
- CN111592155A CN111592155A CN202010359898.7A CN202010359898A CN111592155A CN 111592155 A CN111592155 A CN 111592155A CN 202010359898 A CN202010359898 A CN 202010359898A CN 111592155 A CN111592155 A CN 111592155A
- Authority
- CN
- China
- Prior art keywords
- water
- water supply
- treatment
- medical
- domestic
- 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.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 627
- 238000011282 treatment Methods 0.000 title claims abstract description 107
- 238000000034 method Methods 0.000 title claims abstract description 54
- 239000012528 membrane Substances 0.000 claims abstract description 104
- 239000003651 drinking water Substances 0.000 claims abstract description 83
- 235000020188 drinking water Nutrition 0.000 claims abstract description 83
- 239000000919 ceramic Substances 0.000 claims abstract description 82
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 74
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 73
- 238000001728 nano-filtration Methods 0.000 claims abstract description 64
- 230000008569 process Effects 0.000 claims abstract description 31
- 238000001514 detection method Methods 0.000 claims abstract description 20
- 238000004806 packaging method and process Methods 0.000 claims abstract description 9
- 238000012544 monitoring process Methods 0.000 claims abstract 2
- 238000009296 electrodeionization Methods 0.000 claims description 24
- 238000004659 sterilization and disinfection Methods 0.000 claims description 21
- 238000000746 purification Methods 0.000 claims description 20
- 239000000460 chlorine Substances 0.000 claims description 17
- 239000013505 freshwater Substances 0.000 claims description 17
- 238000003860 storage Methods 0.000 claims description 12
- 238000001471 micro-filtration Methods 0.000 claims description 10
- 238000012372 quality testing Methods 0.000 claims description 9
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 8
- 229910052801 chlorine Inorganic materials 0.000 claims description 8
- 230000001954 sterilising effect Effects 0.000 claims description 8
- 238000010999 medical injection Methods 0.000 claims description 7
- 238000012545 processing Methods 0.000 claims description 7
- 239000003344 environmental pollutant Substances 0.000 claims description 6
- 239000008213 purified water Substances 0.000 claims description 6
- 238000004458 analytical method Methods 0.000 claims description 5
- 231100000719 pollutant Toxicity 0.000 claims description 5
- 238000013461 design Methods 0.000 claims description 4
- 230000002787 reinforcement Effects 0.000 claims description 4
- 239000008215 water for injection Substances 0.000 claims description 4
- 238000012423 maintenance Methods 0.000 claims description 3
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 claims description 2
- 230000009977 dual effect Effects 0.000 claims description 2
- 239000003456 ion exchange resin Substances 0.000 claims description 2
- 229920003303 ion-exchange polymer Polymers 0.000 claims description 2
- 238000000819 phase cycle Methods 0.000 claims description 2
- 238000010248 power generation Methods 0.000 claims description 2
- 238000004088 simulation Methods 0.000 claims description 2
- 238000011221 initial treatment Methods 0.000 claims 2
- 239000002957 persistent organic pollutant Substances 0.000 claims 1
- 230000035939 shock Effects 0.000 claims 1
- 238000005086 pumping Methods 0.000 abstract 1
- 239000000126 substance Substances 0.000 description 56
- 238000004140 cleaning Methods 0.000 description 49
- 239000007788 liquid Substances 0.000 description 16
- 239000000047 product Substances 0.000 description 15
- 238000004519 manufacturing process Methods 0.000 description 14
- 238000004062 sedimentation Methods 0.000 description 14
- 238000000108 ultra-filtration Methods 0.000 description 14
- 238000010979 pH adjustment Methods 0.000 description 12
- 238000005516 engineering process Methods 0.000 description 11
- 150000002500 ions Chemical class 0.000 description 11
- 238000001914 filtration Methods 0.000 description 10
- 229910001385 heavy metal Inorganic materials 0.000 description 10
- 238000006243 chemical reaction Methods 0.000 description 9
- 238000011001 backwashing Methods 0.000 description 7
- 239000007787 solid Substances 0.000 description 6
- 238000012360 testing method Methods 0.000 description 6
- 241000894006 Bacteria Species 0.000 description 5
- 239000005416 organic matter Substances 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 239000010802 sludge Substances 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 239000011572 manganese Substances 0.000 description 4
- 238000001179 sorption measurement Methods 0.000 description 4
- 239000008399 tap water Substances 0.000 description 4
- 235000020679 tap water Nutrition 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 241000588724 Escherichia coli Species 0.000 description 3
- 238000005345 coagulation Methods 0.000 description 3
- 230000015271 coagulation Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000000909 electrodialysis Methods 0.000 description 3
- 238000005189 flocculation Methods 0.000 description 3
- 239000000575 pesticide Substances 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000002242 deionisation method Methods 0.000 description 2
- 238000010612 desalination reaction Methods 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000004907 flux Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- 238000007726 management method Methods 0.000 description 2
- 238000013327 media filtration Methods 0.000 description 2
- 244000000010 microbial pathogen Species 0.000 description 2
- LQNUZADURLCDLV-UHFFFAOYSA-N nitrobenzene Chemical compound [O-][N+](=O)C1=CC=CC=C1 LQNUZADURLCDLV-UHFFFAOYSA-N 0.000 description 2
- 231100000614 poison Toxicity 0.000 description 2
- 230000010287 polarization Effects 0.000 description 2
- 230000002285 radioactive effect Effects 0.000 description 2
- 150000003384 small molecules Chemical class 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000003911 water pollution Methods 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 238000006424 Flood reaction Methods 0.000 description 1
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- 239000006004 Quartz sand Substances 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 1
- 239000003830 anthracite Substances 0.000 description 1
- 229910052785 arsenic Inorganic materials 0.000 description 1
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 1
- 244000052616 bacterial pathogen Species 0.000 description 1
- 230000000721 bacterilogical effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 229930002875 chlorophyll Natural products 0.000 description 1
- 235000019804 chlorophyll Nutrition 0.000 description 1
- ATNHDLDRLWWWCB-AENOIHSZSA-M chlorophyll a Chemical compound C1([C@@H](C(=O)OC)C(=O)C2=C3C)=C2N2C3=CC(C(CC)=C3C)=[N+]4C3=CC3=C(C=C)C(C)=C5N3[Mg-2]42[N+]2=C1[C@@H](CCC(=O)OC\C=C(/C)CCC[C@H](C)CCC[C@H](C)CCCC(C)C)[C@H](C)C2=C5 ATNHDLDRLWWWCB-AENOIHSZSA-M 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 239000002158 endotoxin Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 239000004009 herbicide Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 239000008235 industrial water Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- PNDPGZBMCMUPRI-UHFFFAOYSA-N iodine Chemical compound II PNDPGZBMCMUPRI-UHFFFAOYSA-N 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 238000009285 membrane fouling Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 230000003204 osmotic effect Effects 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000012264 purified product Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000003904 radioactive pollution Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 238000004092 self-diagnosis Methods 0.000 description 1
- 230000001568 sexual effect Effects 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 229910052716 thallium Inorganic materials 0.000 description 1
- BKVIYDNLLOSFOA-UHFFFAOYSA-N thallium Chemical compound [Tl] BKVIYDNLLOSFOA-UHFFFAOYSA-N 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- 230000002110 toxicologic effect Effects 0.000 description 1
- 231100000027 toxicology Toxicity 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 229910021642 ultra pure water Inorganic materials 0.000 description 1
- 239000012498 ultrapure water Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/442—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by nanofiltration
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/463—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrocoagulation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/469—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis
- C02F1/4691—Capacitive deionisation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/76—Treatment of water, waste water, or sewage by oxidation with halogens or compounds of halogens
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/007—Contaminated open waterways, rivers, lakes or ponds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/02—Non-contaminated water, e.g. for industrial water supply
- C02F2103/026—Treating water for medical or cosmetic purposes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/10—Nature of the water, waste water, sewage or sludge to be treated from quarries or from mining activities
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/14—Maintenance of water treatment installations
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/16—Regeneration of sorbents, filters
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Water Treatment By Sorption (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
技术领域technical field
本发明属于水处理设备与工艺技术领域,尤其是涉及可适应各种水源和供电条件,可一站式提供生活 用水、饮用水和医药用水的一种智能型集成式应急水处理装备和方法。The invention belongs to the technical field of water treatment equipment and technology, and particularly relates to an intelligent integrated emergency water treatment equipment and method that can adapt to various water sources and power supply conditions, and can provide domestic water, drinking water and medical water in one stop.
背景技术Background technique
近年来,随着我国社会经济的快速发展和人们生活水平的不断提高,用水量正在呈逐年增加的趋势,对 于水资源的需求量随之上升,这也在一定程度上导致了各类突发性环境污染事件的频繁发生。我国地域辽 阔,地震、洪涝、泥石流等破坏居民家园的重大自然灾害频发。此外,随着人类对自然资源的过度开发和 猎取,生态环境的逐步恶化,全球疫情亦频发。实际上,突发事故、自然灾害或疫情发生时,水资源短缺 以及饮水不安全引起的恐慌和疾病往往造成比灾害、突发事故或疫情本身更可怕的后果。因此,加强应急 水处理装备的开发,保障灾区、疫区生活用水所需、饮水安全以及医药用水的快速供给,提升国家的应 急救灾能力已刻不容缓。In recent years, with the rapid development of my country's social economy and the continuous improvement of people's living standards, the water consumption is showing a trend of increasing year by year, and the demand for water resources is also increasing, which has also led to various emergencies to a certain extent. The frequent occurrence of sexual environmental pollution incidents. my country has a vast territory, and major natural disasters such as earthquakes, floods, and mudslides that destroy the homes of residents frequently occur. In addition, with the over-exploitation and hunting of natural resources by humans, the ecological environment has gradually deteriorated, and global epidemics have also occurred frequently. In fact, when an accident, natural disaster or epidemic occurs, the panic and disease caused by water shortage and unsafe drinking water often have more dire consequences than the disaster, accident or epidemic itself. Therefore, it is imperative to strengthen the development of emergency water treatment equipment to ensure the needs of domestic water, drinking water safety and rapid supply of medical water in disaster-stricken and epidemic areas, and to improve the country's emergency and disaster-relief capabilities.
自然灾害、突发事件多为偶发且不可预测,造成水体污染的因素很多,污染程度不一,直接或间接进 入水体的污染物类型、种类也不同。如我国近20年来发生的“十大水污染事件”中既有砷、镉、铅、铊 等重金属引起的污染,也有化工废水排放引起的苯、硝基苯、氨等化学药剂污染;而切尔诺贝利核事故和 福岛事故则引起核电站附近地表水及海洋的放射性污染;若在战争时期,野外的水源还很可能被化学毒剂、 原子辐射和生物细菌污染。而当自然灾害与突发事件发生时,往往不具备条件也没有太多的时间对水源地 进行选择,这就要求应急水处理装备除具备一般水净化功能外,还应具备对水中不同类型的污染物, 如重金属、农药、化肥、杀虫剂、工业污染、生物污染和放射性污染等的快速去除能力。因此,应急水处理装备必须具有广泛的水源适应性。Natural disasters and emergencies are mostly accidental and unpredictable, and there are many factors that cause water pollution, the pollution levels are different, and the types and types of pollutants that directly or indirectly enter the water body are also different. For example, in the "Top Ten Water Pollution Events" that have occurred in my country in the past 20 years, there are not only pollution caused by heavy metals such as arsenic, cadmium, lead, thallium, etc., but also chemical pollution caused by chemical wastewater discharge such as benzene, nitrobenzene, and ammonia. The Ernobyl nuclear accident and the Fukushima accident have caused radioactive contamination of surface water and oceans near nuclear power plants; during wartime, wild water sources are likely to be contaminated by chemical agents, atomic radiation and biological bacteria. When natural disasters and emergencies occur, there are often no conditions and not much time to choose a water source. This requires emergency water treatment equipment to have the functions of general water purification, as well as different types of water treatment equipment. Rapid removal of pollutants such as heavy metals, pesticides, fertilizers, pesticides, industrial pollution, biological pollution, and radioactive pollution. Therefore, emergency water treatment equipment must have wide adaptability to water sources.
传统自来水厂多采用混凝、沉淀、过滤和消毒的常规水处理工艺,设施多为土建水池,不但占地面积 大,而且建设周期长、维修管理难,不利于抢险救灾和各类军事等大型作业用水。公开号为CN 206069575 U 的中国专利公开了一种集成式一体化净水装置,将传统生活饮用水处理所采用的絮凝、沉淀、过滤三个工 艺段集成在一个矩形箱体内。该工艺虽减小了水处理设施的规模,但处理过程缓慢、出水水质不稳定,处 理能力有限。而应急水处理装备属于一种临时性供水保障装备,要求其应快速启动,迅速产水。Traditional water plants mostly use conventional water treatment processes of coagulation, sedimentation, filtration and disinfection, and most of the facilities are civil pools, which not only cover a large area, but also have a long construction period and difficult maintenance and management, which are not conducive to large-scale rescue and disaster relief and various military projects. Work water. The Chinese Patent Publication No. CN 206069575 U discloses an integrated integrated water purification device, which integrates the three process sections of flocculation, sedimentation and filtration used in traditional drinking water treatment in a rectangular box. Although this process reduces the scale of water treatment facilities, the treatment process is slow, the effluent quality is unstable, and the treatment capacity is limited. The emergency water treatment equipment belongs to a temporary water supply guarantee equipment, and it is required to start up quickly and produce water quickly.
膜法水处理技术具有处理速度快、出水水质优,产水安全性高等特点而在水处理领域得到了较为广泛 的应用。如公开号为CN 104773879 B的中国专利公开了一种集装箱式应急水处理设备及其处理工艺,采 用自清洗过滤器和超滤膜组件相结合的工艺,在超滤膜组件的进出水口前、后均设有压力变送器,可一定 程度上减轻应急使用时,因需快速、大量供水而操作压力过大引起的超滤膜组件易损坏问题;超滤膜组件 出水口浊度仪的设置则能实时检测超滤产水水质。但当水源受到重金属或小分子有机物的污染时,仅利用 超滤膜组件的过滤性能无法获得达标的饮用水,水源适应性不强。Membrane water treatment technology has the characteristics of fast treatment speed, excellent effluent quality, and high safety of produced water, and has been widely used in the field of water treatment. For example, the Chinese patent with publication number CN 104773879 B discloses a container-type emergency water treatment equipment and its treatment process, which adopts the technology of combining a self-cleaning filter and an ultrafiltration membrane module. Before the water inlet and outlet of the ultrafiltration membrane module, There are pressure transmitters at the back, which can reduce to a certain extent the problem of easy damage to the ultrafiltration membrane module caused by excessive operating pressure due to the need for rapid and large water supply in emergency use; the setting of the turbidity meter at the water outlet of the ultrafiltration membrane module It can detect the quality of ultrafiltration water in real time. However, when the water source is polluted by heavy metals or small molecular organic matter, only the filtration performance of the ultrafiltration membrane module cannot obtain drinking water that meets the standard, and the adaptability of the water source is not strong.
为了克服超滤装置对于水中化学污染物、重金属和矿物盐等有害物质去除率低的问题,公开号为CN 207958018 U的中国专利则公开了一种包括管道混合器、二级旋流除砂器、自清洗过滤器、超滤装置、纳 滤装置和消毒装置的移动式应急水处理装备。纳滤装置的设置使得该应急水处理装备运行时对水中的硬度 离子、高价重金属离子、天然有机物、痕量的杀虫剂和除草剂等均具有好的去除效果。但当水源中含有放 射性离子、氟、碘、硝酸根等一价离子,分子量小于200的有毒物质时,纳滤膜的去除能力则受限。In order to overcome the problem that the ultrafiltration device has a low removal rate of harmful substances such as chemical pollutants, heavy metals and mineral salts in water, the Chinese Patent Publication No. CN 207958018 U discloses a pipeline mixer and a secondary cyclone desander. , mobile emergency water treatment equipment for self-cleaning filters, ultrafiltration devices, nanofiltration devices and disinfection devices. The installation of the nanofiltration device enables the emergency water treatment equipment to have a good removal effect on hardness ions, high-value heavy metal ions, natural organic matter, trace amounts of pesticides and herbicides in the water during operation. However, when the water source contains radioactive ions, fluorine, iodine, nitrate and other monovalent ions, and toxic substances with a molecular weight of less than 200, the removal capacity of the nanofiltration membrane is limited.
为了提高应急水处理装备的水源适应性,公开号为CN 105060603 A的中国专利则公开了一种基于多 种污染类型的移动式应急水处理设备及其工艺,采用“预沉袋+磁加载混凝反应器+超滤模块+反渗透和纳 滤模块+杀菌模块”的应急水处理工艺来获得生活饮用水。该专利的主要发明点在于通过预沉袋、磁加载 混凝反应器和竖流沉淀箱相结合的方式加强超滤模块的预处理,以此来提高应急水处理装备的水源适应 性。但预处理模块结构复杂,其中所述的磁加载混凝反应器包括加药系统、混合反应系统和磁回收系统, 所需箱体较多,占用空间大;竖流沉淀箱的出水直接进入后续的超滤系统,中间没有过滤环节,也会影响 超滤膜的使用寿命;各模块间需现场组装、调试,不利于紧急情况下的快速启动;只能获得生活饮用水, 无法满足重大疫情或灾情发生时的大量医药用水需求,无法实现一站式供水。In order to improve the water source adaptability of emergency water treatment equipment, the Chinese Patent Publication No. CN 105060603 A discloses a mobile emergency water treatment equipment and its process based on various types of pollution. Condensation reactor + ultrafiltration module + reverse osmosis and nanofiltration module + sterilization module” emergency water treatment process to obtain drinking water. The main invention of this patent is to strengthen the pretreatment of the ultrafiltration module by combining the pre-settling bag, the magnetic loading coagulation reactor and the vertical flow sedimentation tank, so as to improve the water source adaptability of the emergency water treatment equipment. However, the structure of the pretreatment module is complex, and the magnetically loaded coagulation reactor includes a dosing system, a mixed reaction system and a magnetic recovery system, which require many boxes and occupy a large space; the effluent of the vertical flow sedimentation box directly enters the subsequent There is no filtration link in the middle of the ultrafiltration system, which will also affect the service life of the ultrafiltration membrane; each module needs to be assembled and debugged on site, which is not conducive to rapid startup in emergency situations; only drinking water can be obtained, which cannot meet the requirements of major epidemics or Due to the large demand for medical water during the disaster, one-stop water supply cannot be achieved.
三法净水一体化技术以电絮凝为基础,同时结合沉淀和过滤技术,可有效去除水中的硬度、浊度、胶 体颗粒、悬浮物、重金属离子、氨氮、油类等物质。与其他常规的预处理技术相比,三法净水一体化技术 具有进水指标宽、出水水质好、产水率高、运行费用低、占地面积小的优势,而成功用于焦化厂、炼油厂 和热电厂循环冷却水处理,工业给水处理、反渗透浓水处理等领域。该技术在水处理领域的应用,为膜法 深度水处理提供了保障,但基于此技术的移动式应急水处理设备则未见公开。The three-method water purification integrated technology is based on electroflocculation, combined with sedimentation and filtration technology, which can effectively remove hardness, turbidity, colloidal particles, suspended solids, heavy metal ions, ammonia nitrogen, oils and other substances in water. Compared with other conventional pretreatment technologies, the three-method water purification integrated technology has the advantages of wide influent index, good effluent quality, high water production rate, low operating cost and small footprint, and has been successfully used in coking plants, Refinery and thermal power plant circulating cooling water treatment, industrial water supply treatment, reverse osmosis concentrated water treatment and other fields. The application of this technology in the field of water treatment provides a guarantee for advanced membrane water treatment, but the mobile emergency water treatment equipment based on this technology has not been disclosed.
因此,本发明提出以三法净水一体化系统作为初级预处理,同时集超滤、纳滤、反渗透和电去离子等 技术于一体,开发水源适应性强、产水速度快、移动性好且能够满足多种用水需求的集成式应急供水装备 及方法,对于保障突发事件、自然灾害和疫情发生时的应急供水具有重要的战略意义。Therefore, the present invention proposes to use a three-method water purification integrated system as the primary pretreatment, and integrates technologies such as ultrafiltration, nanofiltration, reverse osmosis, and electrodeionization, so as to develop water sources with strong adaptability, fast water production, and mobility. The integrated emergency water supply equipment and method that is good and can meet a variety of water needs has important strategic significance for ensuring emergency water supply during emergencies, natural disasters and epidemics.
发明内容SUMMARY OF THE INVENTION
本发明的目的在于克服目前国内应急水处理装备无法满足突发事故或重大灾难抢险救援时复杂 多变的水源水质以及不同用水需求的问题。提供一种智能型集成式水处理装备,装备中的生活用水、 饮用水和医药用水供水单元可根据实际的水源水质和用水需求进行优化组合和快速启动,可极大提 高工艺处理效果,节约空间、降低能耗、减少产水的二次污染、增强设备的适用性和整体机动性, 最大限度地保证应急水处理装备的高效运转,满足不同的用水需求,实现一站式供水服务。The purpose of the present invention is to overcome the problem that the current domestic emergency water treatment equipment cannot meet the complex and changeable water source water quality and different water demands during emergency rescue or major disaster rescue. Provide an intelligent integrated water treatment equipment. The domestic water, drinking water and medical water supply units in the equipment can be optimally combined and quickly started according to the actual water quality and water demand, which can greatly improve the process treatment effect and save space. , reduce energy consumption, reduce secondary pollution of produced water, enhance the applicability and overall mobility of equipment, maximize the efficient operation of emergency water treatment equipment, meet different water needs, and achieve one-stop water supply services.
本发明解决其技术问题是通过以下技术方案实现的:The present invention solves its technical problem and realizes through the following technical solutions:
一种智能型集成式应急水处理装备,采用集成化设计,包括预处理单元、生活用水供水单元、饮用水 供水单元、医药用水供水单元、水质检测单元、电力供给单元、智能控制单元。上述的所有单元设备均固 定在一20ft标准集装箱底部,每个单元或者单独运行,或者将多个单元的设备构件串联或并联运行,根 据不同的原水水质和供水需求,对水处理工艺流程进行优化组合,实现应急水处理装备的快速启动和高效 运行。其中水质检测分为原水水质和产品水水质检测两个方面。通过对原水水质检测可以科学地选择水源, 有针对性地选择水处理工艺、合理设定水处理运行参数;产品水水质检测则保证产水达到相应的水质标准。 智能控制单元采用DCS控制系统设计,完成对各单元模块的驱动、切换、运行和停机的控制以及对各种传 感器信号的采集,优化出最佳的工艺流程、最佳的运行状态和最准确的运行数据。An intelligent integrated emergency water treatment equipment adopts an integrated design, including a pretreatment unit, a domestic water supply unit, a drinking water supply unit, a medical water supply unit, a water quality detection unit, a power supply unit, and an intelligent control unit. All the above unit equipment is fixed at the bottom of a 20ft standard container. Each unit operates alone, or the equipment components of multiple units are operated in series or in parallel, and the water treatment process is optimized according to different raw water quality and water supply requirements. Combination to achieve rapid start-up and efficient operation of emergency water treatment equipment. The water quality testing is divided into two aspects: raw water quality and product water quality testing. Through the testing of raw water quality, the water source can be selected scientifically, the water treatment process can be selected in a targeted manner, and the operating parameters of water treatment can be reasonably set; the testing of product water quality can ensure that the produced water meets the corresponding water quality standards. The intelligent control unit adopts the design of the DCS control system, completes the control of the drive, switching, operation and shutdown of each unit module, as well as the acquisition of various sensor signals, and optimizes the best process flow, the best operating state and the most accurate. Operating data.
所述的预处理单元包括原水泵、三法净水一体化装置、消毒装置、供水箱、智能控制元件和管件阀门。The pretreatment unit includes a raw water pump, a three-method water purification integrated device, a disinfection device, a water supply tank, an intelligent control element and a pipe fitting valve.
进一步的,所述原水泵一端经原水泵的进水管道与水源相连,其中原水泵为两套互为备用,根据水源 的不同,启用不同的原水泵。如果水源为清洁的自来水,即启用增压泵,增压泵一端连接原水进水管道, 另一端连接消毒装置进行灭菌消毒后进入供水箱。如果水源为河塘或矿井水等,则启用潜水泵为后续的预 处理设备取水,潜水泵一端连接进水管道,另一端连接三法净水一体化装置。Further, one end of the raw water pump is connected to the water source through the water inlet pipe of the raw water pump, wherein two sets of raw water pumps are used as backup for each other, and different raw water pumps are activated according to different water sources. If the water source is clean tap water, the booster pump is activated. One end of the booster pump is connected to the raw water inlet pipe, and the other end is connected to the disinfection device for sterilization and disinfection, and then enters the water supply tank. If the water source is river pond or mine water, etc., start the submersible pump to take water for the subsequent pretreatment equipment. One end of the submersible pump is connected to the water inlet pipe, and the other end is connected to the three-method water purification integrated device.
进一步的,所述三法净水一体化装置由电絮凝反应池、沉淀池、过滤池和污泥收集池组成。原水泵将 需处理的原水泵入电絮凝反应池处理后进入沉淀池中,在反应池形成的大部分絮凝体经沉淀池沉淀下来, 剩余的少量细小絮体进入过滤池中,除去水中剩余的细小絮体、悬浮物、泥沙、铁锈、大颗粒物等机械杂 质,沉淀池底部的污泥通过沉淀池底部排入污泥收集池。Further, the three-method water purification integrated device is composed of an electroflocculation reaction tank, a sedimentation tank, a filter tank and a sludge collection tank. The raw water pump sends the raw water to be treated into the electro-flocculation reaction tank and then enters the sedimentation tank. Most of the flocs formed in the reaction tank are deposited in the sedimentation tank, and the remaining small amount of fine flocs enter the filter tank to remove the remaining water. Mechanical impurities such as fine flocs, suspended solids, sediment, rust, large particles, etc., the sludge at the bottom of the sedimentation tank is discharged into the sludge collection tank through the bottom of the sedimentation tank.
更进一步的,所述电絮凝反应池内设置电极板加电,在电场的作用下,产生高活性吸附基团,吸附水 中的胶体颗粒、悬浮物、非溶解性有机物、重金属离子、二氧化硅等杂质,形成较大的絮凝体结构从水中 析出。沉淀池采用高效的斜管或斜板沉淀池,其处理能力是平流式沉淀池的3-5倍,污泥沉降性好。过滤 池采用多介质过滤,通过锰砂、无烟煤、石英砂等多介质过滤处理后的出水进入后续的消毒装置。Further, the electrode plate is installed in the electro-flocculation reaction tank to be energized, and under the action of the electric field, highly active adsorption groups are generated to adsorb colloidal particles, suspended solids, insoluble organics, heavy metal ions, silicon dioxide, etc. in the water. Impurities, which form larger floc structures, are precipitated out of the water. The sedimentation tank adopts high-efficiency inclined tube or inclined plate sedimentation tank, and its processing capacity is 3-5 times that of the advective sedimentation tank, and the sludge settleability is good. The filter tank adopts multi-media filtration, and the effluent treated by multi-media filtration such as manganese sand, anthracite, and quartz sand enters the subsequent disinfection device.
进一步的,所述消毒装置可由依次连接的氯消毒器和紫外灭菌器组成,其中所述的氯消毒器通过在水 中添加氯或氯制剂进行消毒,以杀死各种病原微生物,保障产水的安全;所述的紫外灭菌器通过采用高效 率、高强度和长寿命的紫外光发生装置产生强的紫外光照射流水来达到消毒、灭菌的目的。所述供水箱的 入口与消毒装置的出口相连接,用于储存预处理后的水,供水箱的出口与饮用水供水单元的供水泵的入口 相接。Further, the sterilizing device can be composed of a chlorine sterilizer and an ultraviolet sterilizer connected in sequence, wherein the chlorine sterilizer is sterilized by adding chlorine or chlorine preparation to the water to kill various pathogenic microorganisms and ensure the water production. The ultraviolet sterilizer achieves the purpose of disinfection and sterilization by using a high-efficiency, high-intensity and long-life ultraviolet light generating device to generate strong ultraviolet light to irradiate flowing water. The inlet of the water supply tank is connected with the outlet of the disinfection device for storing pretreated water, and the outlet of the water supply tank is connected with the inlet of the water supply pump of the drinking water supply unit.
在预处理单元中,通过DCS的智能控制来实现潜水泵和增压泵之间的互相切换以及三法净水一体化装 置的反冲洗操作。通过预处理单元的运行模式、运行参数和进出水水质对对预处理工艺进行优化,经过预 处理单元处理后的水经供水箱进入后续的生活用水供水单元。In the pretreatment unit, the switch between the submersible pump and the booster pump and the backwash operation of the three-method water purification integrated device are realized through the intelligent control of DCS. The pretreatment process is optimized through the operation mode, operation parameters and water quality of the influent and effluent of the pretreatment unit. The water treated by the pretreatment unit enters the subsequent domestic water supply unit through the water supply tank.
所述的生活用水供水单元包括由管道依次连通的供水泵、活性炭吸附器、精密过滤器、增压泵、陶瓷 膜过滤器和生活用水供水箱。进一步的,所述供水泵一端接预处理单元的供水箱,一端接活性炭吸附器, 活性炭吸附器借助活性炭的吸附作用,去除大分子有机物、余氯等污染物。当进、出口压差在0.05-0.07MPa 时,活性炭吸附器的进、出口阀门会自动切换到反冲洗状态,反冲洗过程结束后,又会自动切换到过滤状 态。活性碳的出口接精密过滤器,主要去除预处理中未能完全去除的悬浮颗粒或防止活性炭吸附器中的细 小微粒进入后续的陶瓷膜过滤器,精密过滤器的过滤精度为5-10μm,当进出口压差大于0.05MPa时更 换滤芯。The domestic water supply unit includes a water supply pump, an activated carbon adsorber, a precision filter, a booster pump, a ceramic membrane filter and a domestic water supply tank which are connected in sequence by pipelines. Further, one end of the water supply pump is connected to the water supply tank of the pretreatment unit, and the other end is connected to an activated carbon adsorber, and the activated carbon adsorber removes pollutants such as macromolecular organic matter and residual chlorine by the adsorption of activated carbon. When the pressure difference between the inlet and the outlet is 0.05-0.07MPa, the inlet and outlet valves of the activated carbon adsorber will automatically switch to the backwashing state. After the backwashing process is over, it will automatically switch to the filtering state. The outlet of the activated carbon is connected to a precision filter, which mainly removes the suspended particles that cannot be completely removed in the pretreatment or prevents the fine particles in the activated carbon adsorber from entering the subsequent ceramic membrane filter. The filtration accuracy of the precision filter is 5-10μm. Replace the filter element when the pressure difference between the inlet and outlet is greater than 0.05MPa.
进一步的,所述陶瓷膜过滤器通过增压泵与精密过滤器出口相接,主要由陶瓷膜组件、反洗系统、化 学清洗系统、自动控制系统、泵、管阀件等组成。运行方式采用循环错流以增大膜表面的液体流速,使膜 表面凝胶层厚度降低,阻止微粒在膜表面的堆积,从而可以有效降低膜的污染,增强膜的通量。采用DCS 程序控制来实现自动与手动的切换。进一步的,陶瓷膜孔径为0.05-0.10μm,允许小分子和溶解性固体 等通过,对悬浮物、细菌、病菌及大分子量胶体物质具有较好的截留作用,过滤出水满足生活用水水质标 准,进入后续的生活用水供水箱进行贮存。Further, the ceramic membrane filter is connected to the outlet of the precision filter through a booster pump, and is mainly composed of a ceramic membrane assembly, a backwashing system, a chemical cleaning system, an automatic control system, a pump, a pipe valve and the like. The operating mode adopts circulating cross-flow to increase the liquid flow rate on the membrane surface, reduce the thickness of the gel layer on the membrane surface, and prevent the accumulation of particles on the membrane surface, thereby effectively reducing membrane fouling and enhancing membrane flux. Adopt DCS program control to realize automatic and manual switching. Further, the pore size of the ceramic membrane is 0.05-0.10 μm, which allows the passage of small molecules and dissolved solids, and has a good interception effect on suspended solids, bacteria, germs and large molecular weight colloidal substances. The filtered water meets the water quality standards for domestic water. Subsequent domestic water supply tanks are stored.
进一步的,所述生活用水供水箱内设有液位传感器和控制阀门,起到贮水和缓冲的作用。生活用水供 水箱上可设有至少一个水龙头,也可通过管道与已有的生活用水设施相连接,以更加便利地为灾区或疫区 民众提供可直接使用的生活用水。同时,生活用水供水箱还设有与后续的饮用水供水单元连接的出水口, 使得生活用水供水箱的另一部分水输送至后续的饮用水供水单元做进一步的深度处理。Further, the domestic water supply tank is provided with a liquid level sensor and a control valve, which play the role of water storage and buffering. The domestic water supply tank can be provided with at least one faucet, and can also be connected to the existing domestic water facilities through pipes, so as to more conveniently provide the people in the disaster area or the epidemic area with domestic water that can be used directly. At the same time, the domestic water supply tank is also provided with a water outlet connected to the subsequent drinking water supply unit, so that another part of the water in the domestic water supply tank is sent to the subsequent drinking water supply unit for further advanced treatment.
所述的饮用水供水单元包括纳滤和反渗透两种深度处理系统。纳滤和反渗透两种深度处理系统可并行 同时工作,也可单独工作。根据水质检测单元的检测结果,采用DCS智能控制,自动运行,在纳滤和反渗 透两种处理系统之间互相切换。The drinking water supply unit includes two advanced treatment systems of nanofiltration and reverse osmosis. The two advanced treatment systems of nanofiltration and reverse osmosis can work in parallel or work independently. According to the detection results of the water quality detection unit, the DCS intelligent control is adopted to automatically operate and switch between the two treatment systems of nanofiltration and reverse osmosis.
所述的纳滤深度处理系统包括依次连接的加压泵、纳滤装置、循环水泵,精制活性炭吸附器,紫外线 灭菌器,微滤装置和饮用水供水箱。The nanofiltration advanced treatment system includes a pressurized pump, a nanofiltration device, a circulating water pump, a refined activated carbon adsorber, an ultraviolet sterilizer, a microfiltration device and a drinking water supply tank connected in sequence.
进一步的,在生活用水供水箱和纳滤装置之间设有加压泵,以提升生活用水供水箱和纳滤装置的送水 压力和效率。Further, a pressurized pump is arranged between the domestic water supply tank and the nanofiltration device to improve the water supply pressure and efficiency of the domestic water supply tank and the nanofiltration device.
进一步的,所述纳滤装置主要由纳滤膜组件、仪表、管线、阀门、加药系统、控制系统和化学清洗等 组成。运行方式采用智能控制,自动运行。所述的纳滤装置采用过滤孔径不超过0.001um的低压选择性纳 滤膜,其孔径范围介于反渗透膜和超滤膜之间,对二价和多价离子及分子量在200-1000之间的有机物和 微污染物有较高的脱除性能,而对单价离子和小分子的脱除率较低。上述的低压选择性纳滤膜具有更低的 工作压力和更高的膜通量,可实现应急装备快速制水的需求。Further, the nanofiltration device is mainly composed of nanofiltration membrane assembly, instrument, pipeline, valve, dosing system, control system, chemical cleaning and the like. The operation mode adopts intelligent control and automatic operation. The nanofiltration device adopts a low-pressure selective nanofiltration membrane with a filtration pore size not exceeding 0.001um, and its pore size range is between the reverse osmosis membrane and the ultrafiltration membrane. The organic matter and micro-pollutants have high removal performance, while the removal rate of monovalent ions and small molecules is low. The above-mentioned low-pressure selective nanofiltration membrane has lower working pressure and higher membrane flux, which can meet the needs of emergency equipment for rapid water production.
进一步的,在纳滤装置出口和精制活性炭吸附器入口间设有循环水泵,提供后续处理所需的压力。经 纳滤装置的出水口依次连接有精制活性炭吸附器,紫外线灭菌器,微滤装置,以确保纳滤产水的安全性和 提升饮用水的口感。经过纳滤系统深度处理后的水满足国家饮用水水质标准,进入后续的饮用水供水箱进 行贮存。Further, a circulating water pump is provided between the outlet of the nanofiltration device and the inlet of the refined activated carbon adsorber to provide the pressure required for subsequent treatment. The water outlet of the nanofiltration device is connected with a refined activated carbon adsorber, an ultraviolet sterilizer, and a microfiltration device in order to ensure the safety of the nanofiltration water and improve the taste of drinking water. The water after advanced treatment by the nanofiltration system meets the national drinking water quality standards and enters the subsequent drinking water supply tank for storage.
当原水中存在分子量小于200的小分子有机毒物、单价的有毒离子或放射性同位素时,纳滤产水则达 不到水质标准。此时可通过预先编制好的DCS智能控制程序启动反渗透深度处理系统。进一步的,反渗透 深度处理系统包括依次连接的高压泵、反渗透装置、紫外线灭菌器和饮用水供水箱。When there are small molecular organic poisons with molecular weight less than 200, monovalent toxic ions or radioisotopes in the raw water, the water produced by nanofiltration cannot meet the water quality standards. At this time, the advanced reverse osmosis treatment system can be started through the pre-programmed DCS intelligent control program. Further, the advanced reverse osmosis treatment system includes a high-pressure pump, a reverse osmosis device, an ultraviolet sterilizer and a drinking water supply tank connected in sequence.
进一步的,所述高压泵一端与生活用水供水箱出口端相连,一端与反渗透装置的入口相连,高压泵的 设置为了进一步提高水的压力,以满足后续反渗透装置产水所需的压力。Further, one end of the high-pressure pump is connected with the outlet end of the domestic water supply tank, and one end is connected with the inlet of the reverse osmosis device.
进一步的,所述反渗透装置主要由反渗透膜组件、管件、压力传感器、电动调节阀组成、加药系统和 控制系统组成。在高于溶液渗透压的压力作用系下,依据溶解扩散的原理,只有溶剂水溶解并透过反渗透 膜,而溶解在水中的绝大部分无机盐、重金属、小分子有机物、放射性核素以及细菌、病毒等被截留,以 达到水质净化的目的。Further, the reverse osmosis device is mainly composed of a reverse osmosis membrane assembly, a pipe fitting, a pressure sensor, an electric regulating valve, a dosing system and a control system. Under the pressure system higher than the osmotic pressure of the solution, according to the principle of dissolution and diffusion, only the solvent water dissolves and passes through the reverse osmosis membrane, while most of the inorganic salts, heavy metals, small molecular organics, radionuclides and Bacteria, viruses, etc. are intercepted to achieve the purpose of water purification.
进一步的,所述紫外线灭菌器的入水口与反渗透装置的出水口相连接,其出水口与饮用水供水箱的入 水口相连接,用于对经反渗透装置深度处理后的水进行消毒处理,起到灭菌、杀死病原微生物的目的。Further, the water inlet of the ultraviolet sterilizer is connected with the water outlet of the reverse osmosis device, and the water outlet is connected with the water inlet of the drinking water supply tank, for sterilizing the water after advanced treatment by the reverse osmosis device. Treatment is for the purpose of sterilizing and killing pathogenic microorganisms.
进一步的,所述饮用水供水箱上可设有至少一个水龙头,以更加便利的为灾区或疫区民众提供饮用水。 也可通过管道与已有的饮用水设施相连接,为灾区或疫区民众提供直饮水。若在交通不便或疫情严重的地 区,为了防止输配水过程中的二次污染,所述饮用水供水箱也可通过管道与后续医药用水供水单元中的袋 装水自动包装装置相连,将饮用水供水箱中的饮用水直接包装成袋,以便于及时运送到需要的地方。Further, at least one tap may be provided on the drinking water supply tank, so as to more conveniently provide drinking water for the people in the disaster area or the epidemic area. It can also be connected to existing drinking water facilities through pipes to provide direct drinking water for people in disaster or epidemic areas. In areas with inconvenient traffic or severe epidemics, in order to prevent secondary pollution during the water distribution process, the drinking water supply tank can also be connected to the automatic packaging device for bagged water in the subsequent medical water supply unit through pipes, so that the drinking water can be The drinking water in the water supply tank is directly packaged into bags for timely delivery to where it is needed.
所述的医药用水供水单元包括医药行业纯化水和医药注射用水两种供水系统。其中医药用水供水单元 中的医药行业纯化水供水系统包括循环水泵、精制活性炭吸附器、紫外线灭菌器、微滤装置、医药用水专 用储罐,袋装水自动包装装置。The medical water supply unit includes two water supply systems, purified water for the pharmaceutical industry and water for medical injection. Among them, the purified water supply system for the pharmaceutical industry in the medical water supply unit includes a circulating water pump, a refined activated carbon adsorber, an ultraviolet sterilizer, a microfiltration device, a special storage tank for medical water, and an automatic packaging device for bagged water.
进一步的,所述循环水泵进水口与饮用水供水箱的出水口端相连,循环水泵的出水口与精制活性炭吸 附器的进水端相连,依次通过活性炭吸附器、紫外线灭菌器和微滤装置,进一步灭菌、消毒处理后流经医 药用水专用储罐进入袋装水自动包装装置。Further, the water inlet of the circulating water pump is connected to the water outlet end of the drinking water supply tank, and the water outlet of the circulating water pump is connected to the water inlet end of the refined activated carbon adsorber. , After further sterilization and disinfection treatment, it flows through the special storage tank for medical water and enters the automatic packaging device for bagged water.
当需要医药注射用水时则通过智能控制单元自动开启医药注射用水供水系统,所述的医药注射用水供 水系统包括电去离子装置增压泵、电去离子装置、循环水泵、精制活性炭吸附器、紫外线灭菌器、微滤装 置、医药用水专用储罐,袋装水自动包装装置。When medical water for injection is needed, the intelligent control unit will automatically open the water supply system for medical injection. Sterilizers, microfiltration devices, special storage tanks for medical water, and automatic packaging devices for bagged water.
进一步的,所述饮用水供水箱和电去离子装置之间设有电去离子装置增压泵为电去离子装置提供所需 水压,其中电去离子装置增压泵进水口与饮用水供水箱的出水口端相连,电去离子装置增压泵的出水口与 电去离子装置入口端相连。Further, an electrodeionization device booster pump is provided between the drinking water supply tank and the electrodeionization device to provide the required water pressure for the electrodeionization device, wherein the electrodeionization device booster pump water inlet is connected to the drinking water supply. The water outlet end of the box is connected, and the water outlet of the booster pump of the electrodeionization device is connected with the inlet end of the electrodeionization device.
进一步的,所述电去离子装置主要由电去离子设备、管线、阀门、仪表和控制系统组成。电去离子是 将电渗析与混床离子交换有机地结合在一起的连续去离子过程。电去离子既利用了离子交换过程的深度除 盐,同时又克服了电渗析过程因发生浓差电极化作用而除盐不彻底的问题。电去离子离子技术利用电渗析 的极化作用发生水的解离,产生的OH-和H+来实现离子交换剂的原位再生,从而使电去离子过程基本上能 够去除水中的全部离子而获得纯水和超纯水。电去离子设备内部浓、淡水室均填充离子交换树脂,运行方 式为自动倒级,倒级时间和冲洗时间可由智能控制单元任意设置。Further, the electrodeionization device is mainly composed of electrodeionization equipment, pipelines, valves, instruments and control systems. Electrodeionization is a continuous deionization process that organically combines electrodialysis and mixed bed ion exchange. Electrodeionization not only utilizes the deep desalination of the ion exchange process, but also overcomes the problem of incomplete desalination due to the concentration electric polarization in the electrodialysis process. Electrodeionization ionization technology utilizes the polarization of electrodialysis to dissociate water, and the generated OH- and H + to achieve in-situ regeneration of ion exchangers, so that the electrodeionization process can basically remove all the ions in the water and Obtain pure and ultrapure water. The concentrated and fresh water chambers of the electrodeionization equipment are filled with ion exchange resin. The operation mode is automatic reversal, and the reversal time and flushing time can be arbitrarily set by the intelligent control unit.
进一步的,袋装水自动包装装置可将医药行业纯化水和医药注射用水分装为容量为100-1000mL的袋 装水,便于灾区或疫区临时医院的救急用水。Further, the bagged water automatic packaging device can pack purified water in the pharmaceutical industry and water for medical injection into bagged water with a capacity of 100-1000mL, which is convenient for emergency water in disaster areas or temporary hospitals in epidemic areas.
所述水质检测单元包括便携式检测仪器和在线分析仪器。其中便携式检测仪器主要有便携式水质检测 仪、检水检毒箱和对放射性核素进行定量检测的便携式射线测量仪,在线分析仪器主要包括在线水质检毒 仪、在线浊度仪、在线余氯分析仪、在线电导率、在线pH计和在线电阻率仪。水质检测分为原水水质检 测和净化处理后的产品水水质检测两个方面。通过对原水水质检测可以科学地选择水源,有针对性地选择 水处理工艺、合理设定水处理运行参数。其中原水水质检测的指标主要包括原水浊度、水温、重金属含量、 叶绿素、有机物含量和含盐量等方面,采用便携式检测仪器进行检测。产品水水质检测尽可能按照国家饮 用水卫生标准、医药行业纯化水和医药注射用水的相关标准进行检测,以保证产品水的安全。产品水水质 检测指标主要包括细菌学指标、毒理学指标、氯化物、总硬度、游离余氯和一般性化学指标等。The water quality detection unit includes a portable detection instrument and an online analysis instrument. Among them, the portable testing instruments mainly include portable water quality detectors, water detection boxes and portable radiometric measuring instruments for quantitative detection of radionuclides. Online analysis instruments mainly include online water quality detectors, online turbidity meters, online residual chlorine Analyzers, On-Line Conductivity, On-Line pH Meters, and On-Line Resistivity Meters. Water quality testing is divided into two aspects: raw water quality testing and purified product water quality testing. Through the testing of raw water quality, the water source can be selected scientifically, the water treatment process can be selected in a targeted manner, and the operating parameters of water treatment can be reasonably set. Among them, the indicators of raw water quality testing mainly include raw water turbidity, water temperature, heavy metal content, chlorophyll, organic matter content and salt content, etc., and are detected by portable testing instruments. The water quality test of product water shall be tested as far as possible in accordance with the national drinking water hygiene standards, the relevant standards of purified water in the pharmaceutical industry and water for medical injection to ensure the safety of product water. Product water quality testing indicators mainly include bacteriological indicators, toxicological indicators, chloride, total hardness, free residual chlorine and general chemical indicators.
所述的智能控制单元主要由DCS控制器、变频器、传感器、计算机系统、运行状态模拟屏和控制柜等 组成。控制方式设有手动控制模式和自动控制模式,整套系统具有连锁保护、相序识别和报警功能。所述 的智能控制单元采用DCS控制系统设计,完成对各单元模块的驱动、切换、运行和停机的控制以及对各种 传感器信号的采集,系统的运行参数、报警、自诊断及其他管理功能集中在CRT上显示,可以完成对整套 工艺运行参数的修改。整个控制系统的最终目的是将水处理装置在连续运行状况下采集到的数据作为依 据,优化出最佳的工艺流程、最佳的运行状态和最准确的运行数据。The intelligent control unit is mainly composed of a DCS controller, a frequency converter, a sensor, a computer system, a running state simulation screen and a control cabinet. The control mode has manual control mode and automatic control mode, and the whole system has interlock protection, phase sequence identification and alarm functions. The intelligent control unit adopts the design of DCS control system, which completes the control of driving, switching, running and stopping of each unit module and the collection of various sensor signals. The system's operating parameters, alarms, self-diagnosis and other management functions are centralized. Displayed on the CRT, the modification of the entire set of process operating parameters can be completed. The ultimate purpose of the entire control system is to optimize the best process flow, the best operating state and the most accurate operating data based on the data collected by the water treatment device under continuous operating conditions.
所述的电力供给单元采用双供电模式,在没有外接电源供应的突发情况下,通过发电系统为所述的应 急水处理装备中的设备、水泵以及智能控制单元供电,以保障突发条件下的各种应急用水需求。The power supply unit adopts a dual power supply mode. In the event of an emergency without external power supply, the power generation system is used to supply power to the equipment, water pump and intelligent control unit in the emergency water treatment equipment to ensure emergency conditions. various emergency water needs.
所述的应急水处理装备中的各个设备间采用软连接,各设备使用标准组件且各组件间通过标准连接件 进行快速连接和组合。进一步的,各组件间通过支撑架连为一体,且与加固架连接。同时,加固架与车辆 通过螺栓防震垫圈连接,以保证所述的应急水处理装备运行、维护方便以及运输过程中的安全性。The various devices in the emergency water treatment equipment are softly connected, each device uses standard components, and each component is quickly connected and combined through standard connectors. Further, the components are connected together through the support frame and connected with the reinforcement frame. At the same time, the reinforcement frame is connected with the vehicle through bolts and shock-proof washers, so as to ensure the convenience of operation and maintenance of the emergency water treatment equipment and the safety during transportation.
本发明的优点和有益效果为:The advantages and beneficial effects of the present invention are:
本发明所提供的智能型集成式应急水处理装备具有水源适应性强、出水水质好、自动化程度高、操作 简便、启动快速、机动性好、可根据水源水质和用水需求对处理工艺进行合理地组合优化的特点。能够把 受化学药剂、重金属、放射性核素、生物细菌和其他有害物质污染的水源或不能直接使用的海水和苦咸水, 由智能控制单元对不同净化工艺间的快速优化组合,分级净化成生活用水、饮用水和医药用水;对于没有 外接电源、没有自来水供应等多种突发条件下仍能适用,可随处快速从最方便的河塘、沟渠、矿井中取水, 水源适应性强;整套水处理设备均集中安装在集装箱内,运输和使用灵活方便,机动性强。同时包含生活 用水、饮用水和医药用水供水单元,可实现灾区或疫区的一站式供水,为临时医院或方舱医院的建设,为 灾情或疫情的防控节省宝贵时间。The intelligent integrated emergency water treatment equipment provided by the invention has the advantages of strong adaptability to water source, good effluent quality, high degree of automation, simple operation, quick start-up, good mobility, and can reasonably carry out the treatment process according to the water source water quality and water demand. Features of combinatorial optimization. It can purify water sources polluted by chemicals, heavy metals, radionuclides, biological bacteria and other harmful substances, or seawater and brackish water that cannot be used directly. Water, drinking water and medical water; it can still be applied to various emergencies such as no external power supply, no tap water supply, etc., and can quickly draw water from the most convenient river ponds, ditches, and mines anywhere, with strong adaptability to water sources; the whole set of water The processing equipment is centrally installed in the container, which is flexible and convenient to transport and use, and has strong mobility. At the same time, it includes domestic water, drinking water and medical water supply units, which can realize one-stop water supply in disaster areas or epidemic areas, save valuable time for the construction of temporary hospitals or makeshift hospitals, and prevent and control disasters or epidemics.
附图说明Description of drawings
图1为本发明的一种智能型集成式应急水处理装备工艺流程示意图;Fig. 1 is a schematic diagram of the process flow of an intelligent integrated emergency water treatment equipment of the present invention;
图2为本发明的一种智能型集成式应急水处理装备的结构示意图;2 is a schematic structural diagram of an intelligent integrated emergency water treatment equipment of the present invention;
图中:In the picture:
预处理单元100、潜水泵101A、增压泵101B、三法净水一体化装置102、电絮凝反应池102A、沉淀池 102B、过滤池102C、污泥收集池102D、消毒装置103、供水箱104、单向阀105、潜水泵出水端控制阀门 106A、增压泵出水端控制阀门106B、潜水泵出水端流量计107A、增压泵出水端流量计107B、潜水泵出水 端压力表108A、增压泵出水端压力表108B、三法净水一体化装置进水口压力开关109、在线浊度仪110、 液位传感器111、供水箱出水控制阀门112、pH调节箱进水控制阀113、pH调节箱114、pH调节控制阀115、 pH调节流量计116、过滤池反冲洗泵117、过滤池反冲洗控制开关118、过滤池反冲洗流量计119、
生活用水供水单元200、供水泵201、活性炭吸附器202、精密过滤器203、增压泵204、陶瓷膜过滤 器205、生活用水供水箱206、供水泵控制阀门207、供水流量计208、供水压力表209、活性炭吸附器进 水压力开关210、陶瓷膜过滤器进水控制阀门211、陶瓷膜过滤器进水流量计212、陶瓷膜过滤器产水阀门 213、在线水质检毒仪214、在线浊度仪215、液位传感器216、生活用水供水阀门217、陶瓷膜过滤器浓 水端低压开关218、陶瓷膜过滤器浓水排放控制阀219、陶瓷膜过滤器浓水排放电磁阀220、陶瓷膜过滤器 反冲洗泵221、陶瓷膜过滤器反冲洗流量控制阀门222、陶瓷膜过滤器反冲洗流量计223、陶瓷膜过滤器反 冲洗水排放阀门224、陶瓷膜过滤器化学清洗箱进水控制开关225、陶瓷膜过滤器化学清洗箱226、陶瓷膜 过滤器化学清洗泵227、陶瓷膜过滤器化学清洗排放开关228、生活用水供水箱出水控制阀门229、Domestic
饮用水供水单元300、加压泵201、纳滤装置302、循环水泵303、精制活性炭吸附器304、紫外线灭 菌器305、微滤装置306、饮用水供水箱307、高压泵308、反渗透装置309、紫外线灭菌器310、纳滤装 置进水控制阀门311、纳滤装置进水流量计312、加药系统313、纳滤装置进水压力表314、纳滤装置产水 压力表315、精制活性炭吸附器进水控制阀门316、纳滤装置浓水排放阀门317、纳滤装置浓水排放流量计 318、饮用水产水控制阀门319、饮用水产水流量计320、在线浊度仪321、在线电导率仪322、液位传感 器323、饮用水供水控制阀门324、纳滤、反渗透装置化学清洗用水开关325、纳滤、反渗透装置化学清洗 用水流量计326、纳滤、反渗透装置化学清洗箱327、纳滤、反渗透装置化学清洗泵328、纳滤、反渗透装 置化学清洗进水控制开关329、纳滤、反渗透装置化学清洗进水流量计330、反渗透装置进水控制阀门331、 反渗透装置进水流量计332、加药系统333、反渗透装置进水压力表334、反渗透装置产水压力表335、反 渗透装置产水控制阀336、反渗透装置浓水排放阀门337、反渗透装置浓水排放流量计338、饮用水供水箱 出水控制阀门339、Drinking water supply unit 300, pressure pump 201, nanofiltration device 302, circulating water pump 303, purified activated carbon adsorber 304, ultraviolet sterilizer 305, microfiltration device 306, drinking water supply tank 307, high pressure pump 308, reverse osmosis device 309, ultraviolet sterilizer 310, nanofiltration device inlet water control valve 311, nanofiltration device inlet water flowmeter 312, dosing system 313, nanofiltration device inlet water pressure gauge 314, nanofiltration device water production pressure gauge 315, refining Activated carbon adsorber inlet water control valve 316, nanofiltration device concentrated water discharge valve 317, nanofiltration device concentrated water discharge flowmeter 318, drinking water production water control valve 319, drinking water production water flowmeter 320, online turbidity meter 321, Online conductivity meter 322, liquid level sensor 323, drinking water supply control valve 324, nanofiltration, reverse osmosis device chemical cleaning water switch 325, nanofiltration, reverse osmosis device chemical cleaning water flow meter 326, nanofiltration, reverse osmosis device chemical Cleaning tank 327, nanofiltration, reverse osmosis device chemical cleaning pump 328, nanofiltration, reverse osmosis device chemical cleaning water inlet control switch 329, nanofiltration, reverse osmosis device chemical cleaning water inlet flowmeter 330, reverse osmosis device water inlet control valve 331, reverse osmosis device inlet water flow meter 332, dosing system 333, reverse osmosis device inlet water pressure gauge 334, reverse osmosis device production water pressure gauge 335, reverse osmosis device production water control valve 336, reverse osmosis device concentrated water discharge valve 337. Reverse osmosis device concentrated water discharge flowmeter 338, drinking water supply tank outlet
医药用水供水单元400、电去离子装置增压泵401、电去离子装置402、循环水泵403、精制活性炭吸 附器404、紫外线灭菌器405、微滤装置406、医药用水专用储罐407、袋装水自动包装装置408、电去离 子装置进水电导率仪409、淡水进水控制开关410A、浓水进水控制开关410B、极水进水控制开关410C、 淡水进水流量计411A、浓水进水流量计411B、极水进水流量计411C、淡水进水压力表412A、浓水进水压 力表412B、极水进水压力表412C、淡水出水在线pH计413A、浓水出水在线pH计413B、淡水出水在线电 导率仪414A、浓水出水在线电导率仪414B、淡水出水在线电阻率仪415、精制活性炭吸附器进水控制开关 416、液位传感器417、医药用水专用储罐出水开关418。Medical
具体实施方式Detailed ways
实施例1Example 1
现结合说明书附图,详细说明本发明的具体实施方式。The specific embodiments of the present invention will now be described in detail with reference to the accompanying drawings.
如图2所示,自来水经过单向阀105后依次通过增压泵101B、增压泵出水端控制阀门106B、增压泵 出水端流量计107B、增压泵出水端压力表108B进入消毒装置103处理后进入供水箱104、其内部设有液 位传感器111;供水箱中所贮存的水通过底部的供水箱出水控制阀门112、供水泵201、供水泵控制阀门 207、供水流量计208、供水压力表209、活性炭吸附器进水压力开关210依次连接进入活性炭吸附器202 进行处理,活性炭吸附器的产水进入精密过滤器203进一步处理,处理后的产水通过管线与增压泵204、 陶瓷膜过滤器进水控制阀门211、陶瓷膜过滤器进水流量计212依次连接后进入陶瓷膜过滤器205,产水 经陶瓷膜过滤器产水阀门213、在线水质检毒仪214、在线浊度仪215后进入生活用水供水箱206,陶瓷膜 过滤器的浓水经过陶瓷膜过滤器的浓水端低压开关218、陶瓷膜过滤器浓水排放控制阀219和陶瓷膜过滤 器浓水排放电磁阀220后排放,生活用水供水箱206中所贮存的部分水经陶瓷膜过滤器反冲洗泵221、陶 瓷膜过滤器反冲洗流量控制阀门222、陶瓷膜过滤器反冲洗流量计223与陶瓷膜过滤器连接,对陶瓷膜过 滤器进行反冲后的水经陶瓷膜过滤器反冲洗水排放阀门224排放;陶瓷膜过滤器需要化学清洗时,陶瓷膜 过滤器205的部分产水经陶瓷膜过滤器化学清洗箱进水控制开关225、陶瓷膜过滤器化学清洗箱226、陶 瓷膜过滤器化学清洗泵227、陶瓷膜过滤器化学清洗排放开关228排出;生活用水供水箱内部设有液位传 感器216,下部设有生活用水供水阀门217提供生活用水;生活用水可通过生活用水供水箱出水控制阀门 229、加压泵301、纳滤装置进水控制阀门311、纳滤装置进水流量计312、加药系统313、纳滤装置进水 压力表314进入纳滤装置302,纳滤装置的产水进入纳滤装置产水压力表315、循环水泵303、精制活性炭 吸附器进水控制阀门316进入精制活性炭吸附器304,纳滤装置的浓水经纳滤装置浓水排放阀门317和纳 滤装置浓水排放流量计318排放;进入精制活性炭吸附器304进行吸附处理后进入紫外线灭菌器305和微 滤装置206处理后依次通过饮用水产水控制阀门319、饮用水产水流量计320、在线浊度仪321、在线电导 率仪322后进入饮用水供水箱307;饮用水供水箱中存贮的水经纳滤、反渗透装置化学清洗用水开关325、 纳滤、反渗透装置化学清洗用水流量计326、纳滤、反渗透装置化学清洗箱327、纳滤、反渗透装置化学 清洗泵328、纳滤、反渗透装置化学清洗进水控制开关329和纳滤、反渗透装置化学清洗进水流量计330 进入纳滤装置302进行化学清洗,饮用水供水箱中设有液位传感器323,饮用水箱内部贮存的水经底部的 饮用水供水控制阀门324提供饮用水。As shown in FIG. 2 , the tap water passes through the
自来水的水质为:pH 7.84,浊度0.38NTU,电导率1124μS/cm,TDS 386mg/L,SO4 2-105.0mg/L, F- 0.69mg/L,Cl- 106.5mg/L,总硬度296mg/L。The water quality of the tap water is: pH 7.84, turbidity 0.38NTU, conductivity 1124μS/cm, TDS 386mg/L, SO 4 2- 105.0mg/L, F - 0.69mg/L, Cl - 106.5mg/L, total hardness 296mg /L.
生活用水水质为:pH 7.74,浊度0.12NTU,电导率1118μS/cm,TDS 380mg/L,SO4 2-103.0mg/L, F- 0.65mg/L,Cl- 103.8mg/L,总硬度266mg/L。The quality of domestic water is: pH 7.74, turbidity 0.12NTU, conductivity 1118μS/cm, TDS 380mg/L, SO 4 2- 103.0mg/L, F - 0.65mg/L, Cl - 103.8mg/L, total hardness 266mg /L.
饮用水供水箱中的水质为:pH 7.65,浊度0.08NTU,电导率125μS/cm,TDS 34.6mg/L,SO4 2- 18.6 mg/L,F- 0.30mg/L,Cl- 37.1mg/L,总硬度14.8mg/L,大肠杆菌未检出,细菌总数0.02CFU/mL,符 合国家饮用水水质标准。The water quality in the drinking water supply tank is: pH 7.65, turbidity 0.08NTU, conductivity 125μS/cm, TDS 34.6mg/L, SO 4 2- 18.6 mg/L, F - 0.30mg/L, Cl - 37.1mg/L L, the total hardness is 14.8mg/L, Escherichia coli is not detected, and the total number of bacteria is 0.02CFU/mL, which meets the national drinking water quality standard.
实施例2Example 2
现结合说明书附图,详细说明本发明的具体实施方式。The specific embodiments of the present invention will now be described in detail with reference to the accompanying drawings.
如图2所示,某矿井水经过单向阀105后依次通过潜水泵101A、潜水泵出水端控制阀门106A、潜水 泵出水端流量计107A,潜水泵出水端压力表108A、三法净水一体化装置进水口压力开关109后进入三法 净水一体化装置102,经三法净水一体化装置102处理后的水通过在线浊度仪110后进入消毒装置103消 毒后进入供水箱104,其内部设有液位传感器111;流经潜水泵控制阀门106A后的水一部分经pH调节箱 进水控制阀113、pH调节箱114、pH调节控制阀115和pH调节流量计116后进入电絮凝反应池102A;需 对过滤池102C进行反冲洗时,供水箱104内贮存的水依次经过滤池反冲洗泵117、过滤池反冲洗控制开关 118、过滤池反冲洗流量计119后进入过滤池102C进行反冲洗;供水箱中贮存的水经底部的供水箱出水控 制阀112与供水泵201、供水泵控制阀门207、供水流量计208、供水压力表209、活性炭吸附器进水压力 开关210依次连接进入活性炭吸附器202进行处理,活性炭吸附器的产水进入精密过滤器203进一步处理, 处理后的产水通过管线与增压泵204、陶瓷膜过滤器进水控制阀门211、陶瓷膜过滤器进水流量计212依 次连接后进入陶瓷膜过滤器205,产水经陶瓷膜过滤器产水阀门213、在线水质检毒仪214、在线浊度仪 215后进入生活用水供水箱206,陶瓷膜过滤器的浓水经过陶瓷膜过滤器的浓水端低压开关218、陶瓷膜过 滤器浓水排放控制阀219和陶瓷膜过滤器浓水排放电磁阀220后排放,生活用水供水箱206中所贮存的部 分水经陶瓷膜过滤器反冲洗泵221、陶瓷膜过滤器反冲洗流量控制阀门222、陶瓷膜过滤器反冲洗流量计 223与陶瓷膜过滤器连接,对陶瓷膜过滤器进行反冲后的水经陶瓷膜过滤器反冲洗水排放阀门224排放; 陶瓷膜过滤器需要化学清洗时,陶瓷膜过滤器205的部分产水经陶瓷膜过滤器化学清洗箱进水控制开关 225、陶瓷膜过滤器化学清洗箱226、陶瓷膜过滤器化学清洗泵227、陶瓷膜过滤器化学清洗排放开关228 排出;生活用水供水箱内部设有液位传感器216,下部设有生活用水供水阀门217提供生活用水;生活用 水可通过生活用水供水箱出水控制阀门229、高压泵308、反渗透装置进水控制阀门331、反渗透装置进水 流量计332、加药系统333、反渗透装置进水压力表334进入反渗透装置309;经反渗透装置处理后的产水 依次通过反渗透装置产水压力表335、反渗透装置产水控制阀336后进入紫外线灭菌器310,灭菌处理后 流经饮用水产水控制阀门319、饮用水产水流量计320、在线浊度仪321、在线电导率仪322后进入饮用水 供水箱307;反渗透装置的浓水经反渗透装置浓水排放阀门337和反渗透装置浓水排放流量计338后排放; 饮用水供水箱中存贮的水经纳滤、反渗透装置化学清洗用水开关325、纳滤、反渗透装置化学清洗用水流 量计326、纳滤、反渗透装置化学清洗箱327,纳滤、反渗透装置化学清洗泵328、纳滤、反渗透装置化学 清洗进水控制开关329和纳滤、反渗透装置化学清洗进水流量计330进入反渗透装置309进行化学清洗;饮用水供水箱中设有液位传感器323,饮用水箱内部贮存的水经底部的饮用水供水控制阀门324提供饮用 水。As shown in Figure 2, after passing through the one-
矿井水的水质为:pH 8.13,浊度95.0NTU,悬浮物5.8mg/L,总硬度395mg/L,TDS2048mg/L,F- 11.2 mg/L,Cl- 141mg/L,NO3 - 22.0mg/L,SO4 2- 213.0mg/L,Fe 0.26mg/L,Mn0.24mg/L,Cu2+ 1.50mg/L。The quality of mine water is: pH 8.13, turbidity 95.0NTU, suspended solids 5.8mg/L, total hardness 395mg/L, TDS 2048mg/L, F - 11.2 mg/L, Cl - 141mg/L, NO 3 - 22.0mg/ L, SO 4 2- 213.0mg/L, Fe 0.26mg/L, Mn 0.24mg/L, Cu 2+ 1.50mg/L.
生活用水供水箱中的水质为:pH 7.41,浊度4.0NTU,总硬度86.1mg/L,TDS 1565mg/L,F- 8.2mg/L, Cl- 132mg/L,NO3 - 20.0mg/L,SO4 2- 186.0mg/L,Fe 0.12mg/L,Mn 0.08mg/L,Cu2+ 1.02mg/L,菌落 总数12CFU/mL。The water quality in the domestic water supply tank is: pH 7.41, turbidity 4.0NTU, total hardness 86.1mg/L, TDS 1565mg/L, F - 8.2mg/L, Cl - 132mg/L, NO 3 - 20.0mg/L, SO 4 2- 186.0mg/L, Fe 0.12mg/L, Mn 0.08mg/L, Cu 2+ 1.02mg/L, total number of colonies 12CFU/mL.
饮用水供水箱中的水质为:pH 7.20,浊度0.02NTU,总硬度30.2mg/L,TDS 180.2mg/L,F- 0.5mg/L, Cl- 15.6mg/L,NO3 - 2.8mg/L,SO4 2- 9.3mg/L,Fe 0.0mg/L,Mn 0.0mg/L,Cu2+0.0mg/L,总大肠杆 菌未检出,菌落总数0.01CFU/mL,符合国家饮用水水质标准。The water quality in the drinking water supply tank is: pH 7.20, turbidity 0.02NTU, total hardness 30.2mg/L, TDS 180.2mg/L, F - 0.5mg/L, Cl - 15.6mg/L, NO 3 - 2.8mg/L L, SO 4 2- 9.3mg/L, Fe 0.0mg/L, Mn 0.0mg/L, Cu 2+ 0.0mg/L, total E. coli was not detected, the total number of colonies was 0.01CFU/mL, in line with the national drinking water quality standard.
实施例3Example 3
现结合说明书附图,详细说明本发明的具体实施方式。The specific embodiments of the present invention will now be described in detail with reference to the accompanying drawings.
如图2所示,某河水经过单向阀105后依次通过潜水泵101A、潜水泵出水端控制阀门106A、潜水泵 出水端流量计107A、潜水泵出水端压力表108A、三法净水一体化装置进水口压力开关109后进入三法净 水一体化装置102,经三法净水一体化装置102处理后的水通过在线浊度仪110后进入消毒装置103消毒 后进入供水箱104,其内部设有液位传感器111;流经潜水泵控制阀门106A后的水一部分经pH调节箱进 水控制阀113、pH调节箱114、pH调节控制阀115和pH调节流量计116后进入电絮凝反应池102A;需对 过滤池102C进行反冲洗时,供水箱104内贮存的水依次经过滤池反冲洗泵117、过滤池反冲洗控制开关 118、过滤池反冲洗流量计119后进入过滤池102C进行反冲洗;供水箱中贮存的水经底部的供水箱出水控制阀112与供水泵201、供水泵控制阀门207、供水流量计208、供水压力表209、活性炭吸附器进水压力 开关210依次连接进入活性炭吸附器202进行处理,活性炭吸附器的产水进入精密过滤器203进一步处理, 处理后的产水通过管线与增压泵204、陶瓷膜过滤器进水控制阀门211、陶瓷膜过滤器进水流量计212依 次连接后进入陶瓷膜过滤器205,产水经陶瓷膜过滤器产水阀门213、在线水质检毒仪214、在线浊度仪 215后进入生活用水供水箱206,陶瓷膜过滤器的浓水经过陶瓷膜过滤器的浓水端低压开关218、陶瓷膜过 滤器浓水排放控制阀219和陶瓷膜过滤器浓水排放电磁阀220后排放,生活用水供水箱206中所贮存的部 分水经陶瓷膜过滤器反冲洗泵221、陶瓷膜过滤器反冲洗流量控制阀门222、陶瓷膜过滤器反冲洗流量计 223与陶瓷膜过滤器连接,对陶瓷膜过滤器进行反冲后的水经陶瓷膜过滤器反冲洗水排放阀门224排放; 陶瓷膜过滤器需要化学清洗时,陶瓷膜过滤器205的部分产水经陶瓷膜过滤器化学清洗箱进水控制开关 225、陶瓷膜过滤器化学清洗箱226、陶瓷膜过滤器化学清洗泵227、陶瓷膜过滤器化学清洗排放开关228 排出;生活用水供水箱内部设有液位传感器216,下部设有生活用水供水阀门217提供生活用水;生活用 水可通过生活用水供水箱出水控制阀门229、高压泵308、反渗透装置进水控制阀门331、反渗透装置进水 流量计332、加药系统333、反渗透装置进水压力表334进入反渗透装置309;经反渗透装置处理后的产水依次通过反渗透装置产水压力表335、反渗透装置产水控制阀336后进入紫外线灭菌器310,灭菌处理后 流经饮用水产水控制阀门319、饮用水产水流量计320、在线浊度仪321、在线电导率仪322后进入饮用水 供水箱307;反渗透装置的浓水经反渗透装置浓水排放阀门337和反渗透装置浓水排放流量计338后排放; 饮用水供水箱中存贮的水经纳滤,反渗透装置化学清洗用水开关325、纳滤、反渗透装置化学清洗用水流 量计326、纳滤、反渗透装置化学清洗箱327、纳滤、反渗透装置化学清洗泵328、纳滤、反渗透装置化学 清洗进水控制开关329和纳滤、反渗透装置化学清洗进水流量计330进入反渗透装置309进行化学清洗; 饮用水供水箱中设有液位传感器323,饮用水箱内部贮存的水经底部的饮用水供水控制阀门324提供饮用 水;饮用水也可通过饮用水供水箱出水控制阀门339、电去离子装置增压泵401、与电去离子装置进水电 导率仪409相连,此后水流分成三股,其中一股作为淡水进水通过淡水进水控制开关410A、淡水进水流量 计411A,淡水进水压力表412A进入电去离子装置402进行处处理后得到的淡水产水流经淡水出水在线pH 计413A,淡水出水在线电导率仪414A,淡水出水在线电阻率仪415;另一股作为浓水通过浓水进水控制开 关410B、浓水进水流量计411B、浓水进水压力表412B进入电去离子装置402,从电去离子装置402的浓 水孔流出的浓水经浓水出水在线pH计413B,浓水出水在线电导率仪414B后排出,还有一股作为极水通过极水进水控制开关410C,极水进水流量计411C、极水进水压力表412C进入电去离子装置402后从极水排 出管线排放,电去离子装置的淡水产水经循环水泵403和进水控制开关416与精制活性炭吸附器404连接, 经活性炭吸附处理后的水进入紫外线灭菌器405和微滤装置406进一步处理后流入医药用水专用储罐407, 医药用水专用储罐内设有液位传感器417,医药用水专用储罐407内部贮存的水经医药用水专用储罐出水 控制阀门418进入袋装水自动包装装置408进行装袋后提供袋装的医药注射用水。As shown in Figure 2, a certain river water passes through the one-
某河水的水质为:pH 7.25,浊度128NTU,电导率150μS/cm,TDS 56mg/L,菌落总数4000CFU/mL。The water quality of a certain river is: pH 7.25, turbidity 128NTU, conductivity 150μS/cm, TDS 56mg/L, total number of colonies 4000CFU/mL.
生活用水供水箱中的水质为:pH 7.12,浊度0.38NTU,电导率138mg/L,TDS 34.6mg/L,SO4 2- 88.6 mg/L,F- 0.52mg/L,Cl- 97.1mg/L,总硬度24.8mg/L,总大肠杆菌未检出,菌落总数12CFU/mL。The water quality in the domestic water supply tank is: pH 7.12, turbidity 0.38NTU, conductivity 138mg/L, TDS 34.6mg/L, SO 4 2- 88.6 mg/L, F - 0.52mg/L, Cl - 97.1mg/L L, the total hardness was 24.8 mg/L, the total E. coli was not detected, and the total number of colonies was 12 CFU/mL.
饮用水供水箱中的水质为:pH 7.05,浊度0.02NTU,电导率13.9μS/cm,SO4 2- 0.58mg/L,F- 0.07 mg/L,Cl- 2.32mg/L,NO3 - 0.36mg/L,菌落总数0.01CFU/mL,符合国家饮用水水质标准。The water quality in the drinking water supply tank is: pH 7.05, turbidity 0.02NTU, conductivity 13.9μS/cm, SO 4 2- 0.58mg/L, F - 0.07 mg/L, Cl - 2.32mg/L, NO 3 - 0.36mg/L, the total number of colonies is 0.01CFU/mL, which meets the national drinking water quality standard.
医药注射用水水质为:pH 6.86,电阻率15.2MΩ.cm,K+ 0.38mg/L,Na+ 0.88mg/L,NH4 +0.10mg/L Zn2+ 0.08mg/L,Cu2+ 0.06mg/L,F- 0.07mg/L,Cl- 0.32mg/L,NO3 - 0.04mg/L,SO4 2-0.04mg/L,细菌 内毒素0CFU/mL,符合中国药典医药用水标准中注射用水水质标准。The water quality of medical injection water is: pH 6.86, resistivity 15.2MΩ.cm, K + 0.38mg/L, Na + 0.88mg/L, NH 4 + 0.10mg/L Zn 2+ 0.08mg/L, Cu 2+ 0.06mg /L, F - 0.07mg/L, Cl - 0.32mg/L, NO 3 - 0.04mg/L, SO 4 2- 0.04mg/L, bacterial endotoxin 0CFU/mL, in line with the Chinese Pharmacopoeia water for injection standard water quality standards.
以上所述仅为本发明的实施例,并非因此限制本发明的专利范围,凡是利用本发明说明书及附图内容 所做的等效结构或等效流程变换,或直接成间接运用在其他相关的技术领域,均同理包括在本发明的专利 保护范围内。The above descriptions are only the embodiments of the present invention, and are not intended to limit the scope of the patent of the present invention. Any equivalent structure or equivalent process transformation made by using the contents of the description and drawings of the present invention, or directly or indirectly applied to other related All technical fields are similarly included in the scope of patent protection of the present invention.
Claims (12)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202010359898.7A CN111592155A (en) | 2020-04-30 | 2020-04-30 | Intelligent integrated emergency water treatment equipment and method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202010359898.7A CN111592155A (en) | 2020-04-30 | 2020-04-30 | Intelligent integrated emergency water treatment equipment and method |
Publications (1)
Publication Number | Publication Date |
---|---|
CN111592155A true CN111592155A (en) | 2020-08-28 |
Family
ID=72189497
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202010359898.7A Pending CN111592155A (en) | 2020-04-30 | 2020-04-30 | Intelligent integrated emergency water treatment equipment and method |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN111592155A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112159030A (en) * | 2020-09-11 | 2021-01-01 | 郑州绿清环保科技有限公司 | Novel leachate treatment system |
CN112479428A (en) * | 2020-11-25 | 2021-03-12 | 武汉理工大学 | Variable drinking water grading treatment intelligent system |
CN112520920A (en) * | 2020-11-26 | 2021-03-19 | 佛山市雅洁源科技股份有限公司 | Method and device for producing and supplying water quickly laid out in field |
CN112591950A (en) * | 2020-12-30 | 2021-04-02 | 佛山市雅洁源科技股份有限公司 | Hospital water monitoring system based on Internet of things |
CN113477084A (en) * | 2021-08-12 | 2021-10-08 | 广州高得环保科技股份有限公司 | Automatic control method and system for pipeline direct drinking water film filtration |
CN114991257A (en) * | 2022-05-13 | 2022-09-02 | 河海大学 | A movable water supply device based on brackish water source and its water supply method |
CN115159620A (en) * | 2022-05-30 | 2022-10-11 | 开能健康科技集团股份有限公司 | Soft water structure and regeneration method thereof |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CH706537A2 (en) * | 2012-05-29 | 2013-11-29 | Ricardo Augusto Fittipaldi Dias | Equipment mobile and compact filtering system for polluted water purification. |
CN105293794A (en) * | 2014-07-18 | 2016-02-03 | 淮安金诺制药设备有限公司 | Device for producing pharmaceutical water |
CN207986857U (en) * | 2018-01-25 | 2018-10-19 | 兰州水森电子科技有限公司 | A kind of water treatment system under particular surroundings |
-
2020
- 2020-04-30 CN CN202010359898.7A patent/CN111592155A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CH706537A2 (en) * | 2012-05-29 | 2013-11-29 | Ricardo Augusto Fittipaldi Dias | Equipment mobile and compact filtering system for polluted water purification. |
CN105293794A (en) * | 2014-07-18 | 2016-02-03 | 淮安金诺制药设备有限公司 | Device for producing pharmaceutical water |
CN207986857U (en) * | 2018-01-25 | 2018-10-19 | 兰州水森电子科技有限公司 | A kind of water treatment system under particular surroundings |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112159030A (en) * | 2020-09-11 | 2021-01-01 | 郑州绿清环保科技有限公司 | Novel leachate treatment system |
CN112479428A (en) * | 2020-11-25 | 2021-03-12 | 武汉理工大学 | Variable drinking water grading treatment intelligent system |
CN112520920A (en) * | 2020-11-26 | 2021-03-19 | 佛山市雅洁源科技股份有限公司 | Method and device for producing and supplying water quickly laid out in field |
CN112591950A (en) * | 2020-12-30 | 2021-04-02 | 佛山市雅洁源科技股份有限公司 | Hospital water monitoring system based on Internet of things |
CN113477084A (en) * | 2021-08-12 | 2021-10-08 | 广州高得环保科技股份有限公司 | Automatic control method and system for pipeline direct drinking water film filtration |
CN114991257A (en) * | 2022-05-13 | 2022-09-02 | 河海大学 | A movable water supply device based on brackish water source and its water supply method |
CN115159620A (en) * | 2022-05-30 | 2022-10-11 | 开能健康科技集团股份有限公司 | Soft water structure and regeneration method thereof |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN111592155A (en) | Intelligent integrated emergency water treatment equipment and method | |
Ikehata et al. | Water recovery from advanced water purification facility reverse osmosis concentrate by photobiological treatment followed by secondary reverse osmosis | |
Wimalawansa | Purification of contaminated water with reverse osmosis: effective solution of providing clean water for human needs in developing countries | |
CN101514060B (en) | Device for treating emergency drinking water | |
US20090289011A1 (en) | Mobile water purification system and method | |
BR102012012827A2 (en) | Compact and mobile filtration equipment and system for polluted water potabilization | |
CN201395538Y (en) | Emergency drinking water treatment equipment | |
CN213537578U (en) | Intelligent integrated emergency water treatment equipment | |
Dheda et al. | Water Treatment for Centre and Home-Based | |
CN111675376A (en) | Integrated intensive distribution type drinking water purification and supply process and device | |
CN203976554U (en) | Packed pure drinking water production device | |
TONG et al. | Water treatment for hemodialysis | |
CN212198858U (en) | Integrated direct drinking water purifier | |
RU153765U1 (en) | INSTALLATION FOR NON-REAGENT WATER TREATMENT | |
CN201864640U (en) | Tap water purifying and activating device | |
CN208279421U (en) | A kind of purified water producing equipment | |
CN222082623U (en) | A smart centralized water supply system for cancer hospitals | |
US11261116B2 (en) | Fluid treatment system | |
KR101685929B1 (en) | Simple water purification appratus having near field communication function for water quality measuring and confirmation | |
CN221588295U (en) | Intelligent centralized quality-classifying water supply system for children in hospital | |
CN202650577U (en) | A decontamination device capable of processing radioactive contamination water into drinking water | |
Trinh | Development of a Decentralized Drinking Water Treatment Plant Based on Membrane Technology for Rural Areas in Vietnam | |
CN201325911Y (en) | On-line monitoring double-membrane water purifying device | |
CN206232513U (en) | A kind of direct drinking water treatment system based on the design of activated carbon filtering technique | |
Darvanjooghi et al. | Modular water treatment practice in cold countries |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20200828 |
|
WD01 | Invention patent application deemed withdrawn after publication |