CN107986506A - A kind of preparation method of flotation fluid, preparation system, purification method and cleaning system - Google Patents
A kind of preparation method of flotation fluid, preparation system, purification method and cleaning system Download PDFInfo
- Publication number
- CN107986506A CN107986506A CN201711467008.9A CN201711467008A CN107986506A CN 107986506 A CN107986506 A CN 107986506A CN 201711467008 A CN201711467008 A CN 201711467008A CN 107986506 A CN107986506 A CN 107986506A
- Authority
- CN
- China
- Prior art keywords
- flotation fluid
- preparation
- flotation
- activated carbon
- cleaning position
- 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
- 238000005188 flotation Methods 0.000 title claims abstract description 105
- 239000012530 fluid Substances 0.000 title claims abstract description 100
- 238000000034 method Methods 0.000 title claims abstract description 42
- 238000004140 cleaning Methods 0.000 title claims abstract description 41
- 238000002360 preparation method Methods 0.000 title claims abstract description 25
- 238000000746 purification Methods 0.000 title claims abstract description 17
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 91
- 238000005189 flocculation Methods 0.000 claims abstract description 40
- 230000016615 flocculation Effects 0.000 claims abstract description 40
- 229910052736 halogen Inorganic materials 0.000 claims abstract description 38
- 150000002367 halogens Chemical class 0.000 claims abstract description 38
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 38
- 238000001914 filtration Methods 0.000 claims abstract description 27
- 230000008569 process Effects 0.000 claims abstract description 26
- 239000012267 brine Substances 0.000 claims abstract description 22
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 claims abstract description 22
- 150000003839 salts Chemical class 0.000 claims abstract description 19
- 239000007788 liquid Substances 0.000 claims abstract description 18
- 239000002994 raw material Substances 0.000 claims abstract description 18
- 239000012528 membrane Substances 0.000 claims abstract description 16
- 239000013049 sediment Substances 0.000 claims abstract description 15
- 238000001179 sorption measurement Methods 0.000 claims abstract description 5
- 238000010521 absorption reaction Methods 0.000 claims abstract description 4
- 238000001704 evaporation Methods 0.000 claims abstract description 3
- 239000002244 precipitate Substances 0.000 claims abstract description 3
- 238000009298 carbon filtering Methods 0.000 claims description 38
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 24
- 238000001471 micro-filtration Methods 0.000 claims description 17
- 239000012535 impurity Substances 0.000 claims description 16
- 238000004062 sedimentation Methods 0.000 claims description 16
- 229910001385 heavy metal Inorganic materials 0.000 claims description 14
- 239000003463 adsorbent Substances 0.000 claims description 13
- 238000004659 sterilization and disinfection Methods 0.000 claims description 12
- 238000007667 floating Methods 0.000 claims description 11
- 229910052751 metal Inorganic materials 0.000 claims description 9
- 239000002184 metal Substances 0.000 claims description 9
- 238000012545 processing Methods 0.000 claims description 9
- 238000005660 chlorination reaction Methods 0.000 claims description 8
- 238000005259 measurement Methods 0.000 claims description 7
- 230000001954 sterilising effect Effects 0.000 claims description 7
- 229910000359 iron(II) sulfate Inorganic materials 0.000 claims description 5
- 239000002245 particle Substances 0.000 claims description 4
- 239000000356 contaminant Substances 0.000 claims description 3
- 239000007787 solid Substances 0.000 claims description 3
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 claims description 2
- 230000000249 desinfective effect Effects 0.000 claims description 2
- 239000008394 flocculating agent Substances 0.000 claims description 2
- 238000006385 ozonation reaction Methods 0.000 claims description 2
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims 1
- 239000010931 gold Substances 0.000 claims 1
- 229910052737 gold Inorganic materials 0.000 claims 1
- 230000000694 effects Effects 0.000 description 15
- 238000004519 manufacturing process Methods 0.000 description 13
- 239000000047 product Substances 0.000 description 10
- 241001131796 Botaurus stellaris Species 0.000 description 8
- 239000011573 trace mineral Substances 0.000 description 8
- 235000013619 trace mineral Nutrition 0.000 description 8
- 229910021578 Iron(III) chloride Inorganic materials 0.000 description 7
- 239000000084 colloidal system Substances 0.000 description 7
- 239000000654 additive Substances 0.000 description 6
- 230000005484 gravity Effects 0.000 description 6
- 229910052500 inorganic mineral Inorganic materials 0.000 description 6
- 235000010755 mineral Nutrition 0.000 description 6
- 239000011707 mineral Substances 0.000 description 6
- 239000011148 porous material Substances 0.000 description 6
- 238000003756 stirring Methods 0.000 description 6
- 238000012360 testing method Methods 0.000 description 6
- 230000006870 function Effects 0.000 description 5
- 230000036541 health Effects 0.000 description 5
- 150000002500 ions Chemical class 0.000 description 5
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 230000002776 aggregation Effects 0.000 description 4
- 238000004220 aggregation Methods 0.000 description 4
- 230000033001 locomotion Effects 0.000 description 4
- 230000004060 metabolic process Effects 0.000 description 4
- 230000000996 additive effect Effects 0.000 description 3
- 238000011161 development Methods 0.000 description 3
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 3
- 239000011777 magnesium Substances 0.000 description 3
- 230000014759 maintenance of location Effects 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 2
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 206010003246 arthritis Diseases 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 201000010099 disease Diseases 0.000 description 2
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000002147 killing effect Effects 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- 210000003205 muscle Anatomy 0.000 description 2
- 230000001151 other effect Effects 0.000 description 2
- 239000011591 potassium Substances 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 208000017520 skin disease Diseases 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 230000002195 synergetic effect Effects 0.000 description 2
- VJFMSYZSFUWQPZ-BIPCEHGGSA-N 4-[(r)-[(2s,4s,5r)-5-ethenyl-1-azabicyclo[2.2.2]octan-2-yl]-hydroxymethyl]quinolin-6-ol Chemical compound C1=C(O)C=C2C([C@H]([C@H]3N4CC[C@H]([C@H](C4)C=C)C3)O)=CC=NC2=C1 VJFMSYZSFUWQPZ-BIPCEHGGSA-N 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- BUGBHKTXTAQXES-UHFFFAOYSA-N Selenium Chemical compound [Se] BUGBHKTXTAQXES-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000001093 anti-cancer Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 230000014461 bone development Effects 0.000 description 1
- 230000008468 bone growth Effects 0.000 description 1
- 210000005013 brain tissue Anatomy 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000001723 curing Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- VJFMSYZSFUWQPZ-UHFFFAOYSA-N demethyl quinine Natural products C1=C(O)C=C2C(C(C3N4CCC(C(C4)C=C)C3)O)=CC=NC2=C1 VJFMSYZSFUWQPZ-UHFFFAOYSA-N 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000011790 ferrous sulphate Substances 0.000 description 1
- 235000003891 ferrous sulphate Nutrition 0.000 description 1
- 210000000987 immune system Anatomy 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 210000004185 liver Anatomy 0.000 description 1
- 230000035800 maturation Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000003534 oscillatory effect Effects 0.000 description 1
- 230000035790 physiological processes and functions Effects 0.000 description 1
- 239000001103 potassium chloride Substances 0.000 description 1
- 235000011164 potassium chloride Nutrition 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 238000001671 psychotherapy Methods 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 238000011084 recovery 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
- 238000009938 salting Methods 0.000 description 1
- 239000011669 selenium Substances 0.000 description 1
- 229910052711 selenium Inorganic materials 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 210000004881 tumor cell Anatomy 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
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
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K35/00—Medicinal preparations containing materials or reaction products thereof with undetermined constitution
- A61K35/02—Medicinal preparations containing materials or reaction products thereof with undetermined constitution from inanimate materials
- A61K35/08—Mineral waters; Sea water
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/96—Cosmetics or similar toiletry preparations characterised by the composition containing materials, or derivatives thereof of undetermined constitution
- A61K8/965—Cosmetics or similar toiletry preparations characterised by the composition containing materials, or derivatives thereof of undetermined constitution of inanimate origin
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61Q—SPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
- A61Q19/00—Preparations for care of the skin
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61Q—SPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
- A61Q19/00—Preparations for care of the skin
- A61Q19/10—Washing or bathing preparations
-
- 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
- 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
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
- C02F1/5245—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents using basic salts, e.g. of aluminium and iron
-
- 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
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/10—Solids, e.g. total solids [TS], total suspended solids [TSS] or volatile solids [VS]
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- 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
Landscapes
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Animal Behavior & Ethology (AREA)
- General Health & Medical Sciences (AREA)
- Public Health (AREA)
- Veterinary Medicine (AREA)
- Epidemiology (AREA)
- Dermatology (AREA)
- Chemical & Material Sciences (AREA)
- Medicinal Chemistry (AREA)
- Pharmacology & Pharmacy (AREA)
- Birds (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Water Treatment By Sorption (AREA)
Abstract
The invention provides a kind of preparation method of flotation fluid, preparation system, purification method and cleaning system.The preparation method of wherein flotation fluid includes the following steps：Step 1, flocculation sediment process, then flocculant and raw material mixed flocculation precipitate；Step 2, filtering adsorption process, liquid carries out filtering absorption into activated carbon filtration system after flocculation sediment；Step 3, ultra-filtration process, the ultrafiltration membrane treatment that the liquid after filtering is adsorbed passes through ultrafiltration system；The nearly saturation strong brine or receive the old halogen after salt that raw material obtains after evaporating brine for beach in the step 1.The invention preparation process is simple, and process efficiency is high and cost is relatively low.
Description
Technical field
The invention belongs to flotation fluid preparation field, more particularly, to a kind of preparation of flotation fluid and Application way.
Background technology
Modern times floating originates from the 1950s, being initially chiefly used in psychotherapy and adjusting intense strain.During floating,
In one environment being isolated from the outside, patient is swum in salting liquid, and water, air are heated to the body of human epidermal by equipment
Temperature-sensitive degree (37 DEG C), the Whole Body heart enter loosening for depth, and consciousness enters the state of " nihility " and " blank ".In flotation process
In, the burden that centrifugal force is brought to human body has been cast aside, whole-body muscle can thoroughly be loosened.By the psychology of more than 50 years
Learning clinical research and technology maturation process, flotation technique is gradually improved and is upgraded, as a kind of brand-new Curing Method, by
The commercial operation stage is gradually entered into, but the flotation fluid floated in health experience domestic at present is usually by different salt components or difference
Traditional Chinese medicine ingredients, which are blent, to be formed.
China's bittern or old halogen yield are very abundant, by taking Binhai New Area in Tianjin as an example, the annual load of Hangu saltern salt manufacturing one
T of negative 280,000 t of crude salt production task~300,000 or so, its old halogen stock number is every year in 350,000 m3~40 ten thousand m3Left and right, old halogen in it
Conveying and eastern halogen it is western it is defeated influenced farther out and by precipitation with permeating etc. because of road, old halogen resource be lost in receipts and course of conveying are got rid of compared with
Big and second-rate, the rate of recovery is relatively low, is 35% or so through one old halogen amount of loss of actual production measuring and calculating salt manufacturing, old halogen resource is not
Fully it can be recycled and be utilized.
Bittern or old halogen contain abundant potassium, magnesium, calcium, sodium resource, but the utilization of China's bittern or old halogen resource at present is only
Simple chemical products can be produced, such as agricultural potassium chloride, industrial hex-ammoniate, calcium chloride, sodium chloride, enrich in bittern or old halogen
Resource do not obtain sufficiently effective utilization, do not form large-scale industrial chain yet, cause to have many saltern beaches to be shone
The bittern or old halogen formed after salt is not developed well, and is flow back to Yan He again, causes bittern or old halogen to provide
The waste and environmental pollution in source.
According to statistics, it is rich in the element being had been detected by several mineral materials and trace element, with human body in bittern or old halogen
It is basically identical.On the 4th, whole nation trace element and healthy discussion, 600 multidigit experts and scholars propose mankind nowadays disease
More than 90% is related with trace element is lacked.Every kind of mineral matter and trace element have human body its special physiological function, ore deposit
Material and microelement deficiencies can give rise to diseases.As sodium maintains human body pH, participation human metabolism, to muscle and heart
Activity plays regulatory role；Potassium maintains acid-base balance, participates in energetic supersession and maintains nervimuscular normal function；Magnesium is almost joined
All metabolic processes with human body, maintain human-body biological film potential；Calcium is " Source of life ", to bone growth and development and life
Reason function point analysis plays an important roll；Copper is blood, liver, the part of brain tissue cuprein；Zinc can enhancing development
And regeneration；Selenium is the essential element of anticancer in immune system, can promote generated human antibody direct killing tumour cell
Deng.
For the above situation, bittern or old halogen resources development and utilization are combined by patent of the present invention with floating health industry,
Old halogen is raw material after nearly saturation strong brine or receipts salt after being evaporated brine using beach, a kind of creative preparation method of flotation fluid of proposition.
Through process such as flocculation sediment, activated carbon filtering, ultrafiltration, the flotation fluid of acquisition is 1.1~1.3g/cm of density3Highly concentrated salt
Water.Matched by the floatation device with independent research, human body lies low in the floatation device added with flotation fluid, by liquid
Buoyancy is in floating state, and flotation fluid penetrates into vivo by concentration difference, and energy, mineral matter and trace element etc. are provided for human body,
By the synergistic effect of energy, mineral matter and trace element, promote human metabolism, recover skin activity, have and highlight skin
Color, deep layer cleaning, firm skin, treatment of arthritis and skin disease and other effects.Preparation process is natural, green without any additive
Color, safe and reliable, healthy health product.The flotation fluid after use is handled using filtration, purification sterilization process, is realized
Being repeatedly circulated of flotation fluid, reduces the use cost of flotation fluid, improves the safety in utilization of flotation fluid.
The content of the invention
In view of this, first purpose of the invention is directed to a kind of method prepared by flotation fluid, through flocculation sediment,
Flotation fluid is obtained after the process such as activated carbon filtering, ultrafiltration, preparation process is simple, and process efficiency is high and cost is relatively low.
To reach above-mentioned purpose, what the technical solution of the invention was realized in：
A kind of method prepared by flotation fluid, includes the following steps：
Step 1, flocculation sediment process, then flocculant and raw material mixed flocculation precipitate；
Step 2, filtering adsorption process, liquid carries out filtering absorption into activated carbon filtration system after flocculation sediment；
Step 3, ultra-filtration process, the ultrafiltration membrane treatment that the liquid after filtering is adsorbed passes through ultrafiltration system；
The nearly saturation strong brine or receive the old halogen after salt that raw material beach obtains after evaporating brine in the step 1.
Preferably, the flocculant in the step 1 is Ferric Salt Flocculants or aluminum salt flocculant, such as can be FeCl3
Or FeSO4Flocculant；
Preferably, the flocculation sediment process in the step 1 specifically includes, raw material is passed first into the flocculation with stirring
Pond, adds flocculant into flocculation basin, occurs to enter sedimentation basin after flocculation reaction, suspended impurity, colloid in raw material and is harmful to
Heavy metal is assembled in sedimentation basin to be formed bulky grain and settles under the effect of gravity.
Preferably, the activated carbon in activated carbon filtration system in the step 2 is cylindrical particulate, granularity exists
Between 0.4~2.5mm, specific surface area is 450~1500m2/ g, pore total measurement (volume) are 0.57~1.15m3/g；
Preferably, the aperture of ultrafiltration membrane in the step 3 is 0.001~0.01 μm, operating pressure for 0.05MPa~
0.1MPa.The operating pressure of selection can farthest reduce process costs while final products parameter is met.
Preferably, when production water Baume degrees reaches 22~30 ° of B é after the ultra-filtration process processing Jing Guo the step 3,
As flotation fluid qualified products.
Second purpose of the invention is to provide a kind of floating liquid preparing system, including the following dress being sequentially communicated
Put：
Flocculation sedimentation tank, for raw material flocculation treatment；
Sedimentation basin, for the particle produced after flocculation treatment to be settled and separated；
Active carbon filtering device, for adsorbing contaminant and heavy metal,
Ultrafiltration apparatus, for retaining suspended matter and solid impurity.
3rd purpose of the invention is to propose a kind of flotation fluid purification method, recycles flotation fluid.
To reach above-mentioned purpose, what the technical solution of the invention was realized in：
A kind of flotation fluid purification method, includes the following steps：
Step S1, microfiltration process, the flotation fluid after use are handled by microfiltration systems；
Step S2, filter process, the flotation fluid after micro-filtration processing are handled by activated carbon filtration system；
Step S3, disinfecting process, the flotation fluid after the processing of activated carbon filtration system are carried out disinfection by chlorination equipment.
Preferably, the chlorination equipment is ozonization plant.
4th purpose of the invention is to provide a kind of floating liquid purification system, including the following dress being sequentially communicated
Put：
Micro-filtration, for carrying out micro-filtration processing to the flotation fluid after use, retention human body flotation process falls into flotation fluid
In dirt, hair etc.；
Active carbon filtering device, for decolourizing to flotation fluid, colority of water is produced less than 15 after realizing decoloration；
Chlorination equipment, for carrying out disinfection to flotation fluid.
Flotation fluid realizes purification after disinfection, can continue to recycle.
As a kind of preferable embodiment, the active carbon filtering device is specifically included such as lower structure：
Adsorbent is equipped with the top of the active carbon filtering device and adds mouth and flotation fluid entrance, is internally provided with cleaning position,
The cleaning position periphery and the active carbon filtering device elastic connection；The cleaning position is internally provided with filter plate, its bottom two
Side is equipped with vibrating motor, its bottom centre exports equipped with flotation fluid, and the flotation fluid is exported through the active carbon filtering device
The hole of bottom extends downwardly.
Preferably, annular sterilizing viltalight lamp is equipped with below the filter plate.
Preferably, the adsorbent, which is added below mouth and flotation fluid inlet port, is equipped with water conservancy diversion inclined-plane, the water conservancy diversion inclined-plane
Bottom is by the first elastic hose with being connected at the top of the cleaning position.The water conservancy diversion inclined-plane to enter cleaning position adsorbent and
Flotation fluid has guide functions so that above-mentioned material rapidly enters；First elastic hose plays slow for cleaning position vibration
Punching, ensures the relative movement of cleaning position.
Preferably, the flotation fluid outlet tip is connected by the second elastic hose with the cleaning position, its bottom
The position for extending the active carbon filtering device is radially vertically equipped with baffle, and the baffle upper surface is equipped with cushioning piece.
Preferably, the cleaning position periphery is connected by multiple metal bracelets with the active carbon filtering device inner wall,
The length of the metal bracelet is longer than the distance of the cleaning position outer wall and the active carbon filtering device inner wall.
Relative to the prior art, the invention has the advantage that：
(1) nearly saturation strong brine or old halogen after salt is received after preferable raw material is evaporated brine for beach, raw material is cheap and easy to get.
(2) it is simpler compared with the prior art for flocculation sediment, activated carbon filtering and ultrafiltration, technique to float liquid preparing process
Single, manufacturing cost is relatively low.
(3) flocculant is ferric trichloride or ferrous sulfate, can remove heavy metal contained in raw material, avoids saturation strong brine
Or the heavy metal in old halogen has an impact health.
(4) flotation fluid prepared is density about 1.1~1.3g/cm3High strong brine, colourity be no more than 15, turbidity 0；
The flotation fluid being prepared can provide energy, mineral matter and trace element etc. for human body, by energy, mineral matter and trace element
Synergistic effect, promote human metabolism, recover skin activity, have bright color, deep layer cleaning, firm skin, treatment
Arthritis and skin disease and other effects, are natural leisure health products.
Brief description of the drawings
Fig. 1 is a kind of preparation method system flow chart of flotation fluid described in the invention；
Fig. 2 is the purification method and system flow chart of a kind of flotation fluid described in the invention
Fig. 3 is the active carbon filtering device structure diagram described in the invention.
Wherein：
1- active carbon filtering devices；10- cleaning positions；101- metal bracelets；102- filter plates；103- annular sterilizations are ultraviolet
Lamp；104- vibrating motors；11- adsorbents add mouth；12- flotation fluid inlet ports；13- is exported；The second elastic hoses of 131-；132-
Baffle；133- cushioning pieces；14- water conservancy diversion inclined-plane；The first elastic hoses of 141-
Embodiment
In addition to being defined, technical term used has and the invention one of ordinary skill in the art in following embodiments
The identical meanings being commonly understood by.Test reagent used, is routine biochemistry reagent unless otherwise specified in following embodiments；
The experimental method, is conventional method unless otherwise specified.
Come that the present invention will be described in detail creates with reference to embodiment and attached drawing.
Embodiment 1
A kind of preparation method of flotation fluid, includes the following steps：
Closely saturation strong brine initially enters the flocculation basin with stirring after step 1, beach are evaporated brine, while is added into flocculation basin
Flocculant FeCl3, FeCl3Additive amount is 28mg/L, subsequently into sedimentation basin, suspended impurity, colloid and harmful weight in strong brine
Metal is assembled in sedimentation basin to be formed bulky grain and settles under the effect of gravity；
Nearly saturation strong brine after step 2, flocculation sediment enters activated carbon filtration system, and activated carbon can further adsorb dense
Impurity, heavy metal in brine, while realize decoloration, operating pressure is 0.1~0.15MPa, and activated carbon used is cylinder
Shape graininess, granularity 0.8mm, specific surface area 1340m2/ g, pore total measurement (volume) are 1.01m3/g；
Production water after step 3, activated carbon filtering enters ultrafiltration system with pump, is removed and suspended using the crown_interception of ultrafiltration membrane
Thing impurity and residual activity carbon powder, the aperture of ultrafiltration membrane is about 0.001~0.01 μm, operating pressure for 0.05MPa~
0.1MPa
It is flotation fluid qualified products when ultrafiltration production water Baume degrees reaches 22~30 ° of B é；
After testing, the leading ion content in the flotation fluid being prepared in the above method is：Ca2+50~500mg/L,
Mg2+20000~40000mg/L, K+300~8000, Na+20000~80000, Cl-100000~230000mg/L, SO4 2-
20000~80000mg/L, 220000~400000mg/L of TDS.
Present invention also provides a kind of preparation system of flotation fluid, as shown in Figure 1, including：
Including the following device being sequentially communicated：
Flocculation sedimentation tank, for raw material flocculation treatment；
Sedimentation basin, for the particle produced after flocculation treatment to be settled and separated；
Active carbon filtering device, for adsorbing contaminant and heavy metal,
Ultrafiltration apparatus, for retaining suspended matter and solid impurity.
Embodiment 2
A kind of flotation fluid purification method, includes the following steps：
Step S1, microfiltration systems are initially entered with rear flotation fluid, micro-filtration membrane aperture is about 0.01~10 μm, microfiltration systems
Operating pressure is 0.1~0.15MPa, dirt, the hair etc. that retention human body flotation process falls into the water；
Step S2, flotation fluid enters activated carbon filtration system after micro-filtration, activated carbon system operating pressure for 0.05~
0.1MPa, main function are decolourized to flotation fluid, and colority of water is produced less than 15 after realizing decoloration；
Step S3, the flotation fluid after activated carbon filtering is carried out disinfection by ozone generating-device, and circulation can be achieved after disinfection
Use.
A kind of cleaning system of flotation fluid is additionally provided in the present embodiment,
Including the following device being sequentially communicated：
Micro-filtration, for carrying out micro-filtration processing to the flotation fluid after use, retention human body flotation process falls into flotation fluid
In dirt, hair etc.；
Active carbon filtering device, for decolourizing to flotation fluid, colority of water is produced less than 15 after realizing decoloration；
Chlorination equipment, for carrying out disinfection to flotation fluid.
Flotation fluid realizes purification after disinfection, can continue to recycle.
As a kind of preferable embodiment, the active carbon filtering device is specifically included such as lower structure：
The top of active carbon filtering device 1 is equipped with adsorbent and adds mouth 11 and flotation fluid inlet port 12, is internally provided with
Cleaning position 10,10 periphery of cleaning position and 1 elastic connection of active carbon filtering device, elastic connection is to ensure to purify
Storehouse 10 vibration when can be opposite movement；The cleaning position 10 is internally provided with filter plate 102, its two bottom sides is equipped with vibration electricity
Machine 104, its bottom centre are equipped with flotation fluid outlet 13, and the flotation fluid outlet 13 passes through 1 bottom of active carbon filtering device
Hole extend downwardly.
Above-mentioned adsorbent and flotation fluid add mouth 11 by adsorbent respectively and flotation fluid inlet port 12 enters cleaning position 10.
The preferred activated carbon of adsorbent, activated carbon have very big specific surface area, to the inorganic or organic substance and colloid in gas, solution
Particle etc. has good adsorption capacity；Cleaning position 10 vibrates under the action of vibrating motor 104, to internal adsorbent and drift
Supernatant liquid fully mixes, and increases contact probability, improves adsorption efficiency, and efficient absorption purification is carried out to flotation fluid.
It is preferably carried out above-mentioned in mode, the lower section of filter plate 102 is equipped with annular sterilizing viltalight lamp 103.The ring
Shape sterilizing viltalight lamp 103 has various bacteriums and microorganism in flotation fluid etc. stronger killing effect, improves flotation fluid and follows
The security that ring uses.
Preferably, it can be equipped with outside the annular sterilizing viltalight lamp 103 and be capable of the waterproof of printing opacity or take others
Waterproof measure, the waterproof can select commercially available waterproof cover body, its concrete shape and material are not restricted.
It is preferably carried out above-mentioned in mode, the adsorbent adds mouth 11 and the lower section of flotation fluid inlet port 12 is equipped with water conservancy diversion
Inclined-plane 14,14 bottom of water conservancy diversion inclined-plane are connected by the first elastic hose 141 with the top of cleaning position 10.The water conservancy diversion
Inclined-plane 14 has guide functions to the adsorbent and flotation fluid that enter cleaning position 10 so that above-mentioned material rapidly enters；Described
One elastic hose 141 plays buffering for the vibration of cleaning position 10, ensures the relative movement of cleaning position 10.
Be preferably carried out above-mentioned in mode, the flotation fluid export 13 tops by the second elastic hose 131 with it is described
Cleaning position 10 is connected, and the position that the active carbon filtering device 1 is extended in its bottom is radially vertically equipped with baffle 132, institute
State 132 upper surface of baffle and be equipped with cushioning piece 133.In 10 oscillatory process of cleaning position, the baffle 132 is to 10 bottom of cleaning position
Flotation fluid outlet 13 play the role of screens, keep the relative stability of flotation fluid outlet 13,13 output exported easy to supernatant liquid
End is connected fixing with 4 flotation fluid of water tank inlet and outlet 42.
It is preferably carried out above-mentioned in mode, 10 periphery of cleaning position passes through multiple metal bracelets 101 and the activity
1 inner wall of charcoal filtration apparatus connects, and the length of the metal bracelet 101 is longer than 10 outer wall of cleaning position and activated carbon filtering
The distance of 1 inner wall of device.The length of wherein described metal bracelet 101 is longer than 10 outer wall of cleaning position and activated carbon filtering
The distance of 1 inner wall of device, be for vibrating motor 104 during the work time, cleaning position 10 is relative to 1 phase of active carbon filtering device
To movement；The metal bracelet 101 has the bearing capacity of bigger than general flexible connector, ensures that cleaning position 10 was vibrating
Cheng Zhongke is withstood forces.
Flotation fluid after micro-filtration processing is passed through the activated carbon by the flotation fluid inlet port 12
In filtration apparatus, after activated-carbon device is handled, flotation fluid is realized after carrying out disinfection into the chlorination equipment
Purification.
Embodiment 3
One kind floating liquid and preparation method thereof, specifically comprises the following steps：
Nearly saturation strong brine after step 1, beach are evaporated brine initially enters the flocculation basin with stirring, while adds into flocculation basin
Add flocculant FeSO4, additive amount 30mg/L, subsequently into sedimentation basin, suspended impurity, colloid and a harmful huge sum of money in strong brine
Belong to the aggregation in sedimentation basin to form bulky grain and settle under the effect of gravity；
Nearly saturation strong brine after step 2, flocculation sediment enters activated carbon filtration system, and activated carbon can further adsorb dense
Impurity, heavy metal in brine, while realize decoloration, operating pressure is 0.1~0.15MPa, and activated carbon used is cylinder
Shape graininess, granularity 1.25mm, specific surface area 980m2/ g, pore total measurement (volume) are 0.83m3/g；
Production water after step 3, activated carbon filtering enters ultrafiltration system with pump, is removed and suspended using the crown_interception of ultrafiltration membrane
Thing impurity and residual activity carbon powder, the aperture of ultrafiltration membrane is about 0.001~0.01 μm, operating pressure for 0.05MPa~
0.1MPa；
It is flotation fluid qualified products when ultrafiltration production water Baume degrees reaches 22~30 ° of B é；
After testing, the leading ion content in the flotation fluid obtained using the above method is：Ca2+50~500mg/L, Mg2+
20000~40000mg/L, K+300~8000, Na+20000~80000, Cl-100000~230000mg/L, SO4 2-20000~
220000~400000mg/L of 80000mg/L, TDS.
Embodiment 4
Old halogen is raw material after the middle salt using receipts in the preparation method of the present embodiment flotation fluid, is comprised the following steps that：
Old halogen initially enters the flocculation basin with stirring after step 1, receipts salt, while flocculant is added into flocculation basin
FeCl3, FeCl3Additive amount is 30mg/L, and subsequently into sedimentation basin, the suspended impurity, colloid and harmful heavy metal in old halogen are heavy
Aggregation forms bulky grain and settles under the effect of gravity in the pond of shallow lake；
Old halogen after step 2, flocculation sediment enters activated carbon filtration system, and activated carbon can further adsorb miscellaneous in old halogen
Matter, heavy metal, while realize decoloration, operating pressure are 0.1~0.15MPa, and activated carbon used is cylindrical particulate, grain
Spend for 1.1mm, specific surface area 1100m2/ g, pore total measurement (volume) are 0.92m3/g；
Old halogen after step 3, activated carbon filtering enters ultrafiltration system with pump, is removed and suspended using the crown_interception of ultrafiltration membrane
Thing impurity and residual activity carbon powder, the aperture of ultrafiltration membrane is 0.001~0.01 μm, and operating pressure is 0.05MPa~0.1MPa；
It is flotation fluid qualified products when ultrafiltration production water Baume degrees reaches 22~30 ° of B é；
After testing, the leading ion content in the flotation fluid that the above method obtains is：Ca2+50~500mg/L, Mg2+
20000~40000mg/L, K+300~8000, Na+20000~80000, Cl-100000~230000mg/L, SO4 2-
20000~80000mg/L, 220000~400000mg/L of TDS.
Embodiment 5
Old halogen is raw material after the middle salt using receipts in the preparation method of the present embodiment flotation fluid, is comprised the following steps that：
Old halogen initially enters the flocculation basin with stirring after step 1, receipts salt, while flocculant is added into flocculation basin
FeCl3, FeCl3Additive amount is 30mg/L, and subsequently into sedimentation basin, the suspended impurity, colloid and harmful heavy metal in old halogen are heavy
Aggregation forms bulky grain and settles under the effect of gravity in the pond of shallow lake；
Old halogen after step 2, flocculation sediment enters activated carbon filtration system, and activated carbon can further adsorb miscellaneous in old halogen
Matter, heavy metal, while realize decoloration, operating pressure are 0.1~0.15MPa, and activated carbon used is cylindrical particulate, grain
Spend for 1.1mm, specific surface area 1100m2/ g, pore total measurement (volume) are 0.92m3/g；
Old halogen after step 3, activated carbon filtering enters ultrafiltration system with pump, is removed and suspended using the crown_interception of ultrafiltration membrane
Thing impurity and residual activity carbon powder, the aperture of ultrafiltration membrane is about 0.001~0.01 μm, operating pressure for 0.05MPa~
0.1MPa；
It is flotation fluid qualified products when ultrafiltration production water Baume degrees reaches 22~30 ° of B é；
After testing, the leading ion content in flotation fluid is：Ca2+50~500mg/L, Mg2+20000~40000mg/
L、K+300~8000, Na+20000~80000, Cl-100000~230000mg/L, SO4 2-20000~80000mg/L,
220000~400000mg/L of TDS.
Embodiment 6
Old halogen is raw material after the middle salt using receipts in the preparation method of the present embodiment flotation fluid, is comprised the following steps that：
Old halogen initially enters the flocculation basin with stirring after step 1, receipts salt, while flocculant is added into flocculation basin
FeSO4, additive amount 40mg/L, subsequently into sedimentation basin, the suspended impurity, colloid and harmful heavy metal in old halogen are in sedimentation basin
Middle aggregation forms bulky grain and settles under the effect of gravity；
Old halogen after step 2, flocculation sediment enters activated carbon filtration system, and activated carbon can further adsorb miscellaneous in old halogen
Matter, heavy metal, while realize decoloration, operating pressure are 0.1~0.15MPa, and activated carbon used is cylindrical particulate, grain
Spend for 1.5mm, specific surface area 820m2/ g, pore total measurement (volume) are 0.72m3/g；
Old halogen after step 3, activated carbon filtering enters ultrafiltration system with pump, is removed and suspended using the crown_interception of ultrafiltration membrane
Thing impurity and residual activity carbon powder, the aperture of ultrafiltration membrane is 0.001~0.01 μm, and operating pressure is 0.05MPa~0.1MPa；
It is flotation fluid qualified products when ultrafiltration production water Baume degrees reaches 22~30 ° of B é；
After testing, it is using the leading ion content in the flotation fluid of above method preparation：Ca2+50~500mg/L, Mg2 +20000~40000mg/L, K+300~8000, Na+20000~80000, Cl-100000~230000mg/L, SO4 2-
20000~80000mg/L, 220000~400000mg/L of TDS.
The foregoing is merely the preferred embodiment of the invention, is not intended to limit the invention creation, all at this
Within the spirit and principle of innovation and creation, any modification, equivalent replacement, improvement and so on, should be included in the invention
Protection domain within.
Claims (9)
- A kind of 1. preparation method of flotation fluid, it is characterised in that：Include the following steps：Step 1, flocculation sediment process, then flocculant and raw material mixed flocculation precipitate；Step 2, filtering adsorption process, liquid carries out filtering absorption into activated carbon filtration system after flocculation sediment；Step 3, ultra-filtration process, the ultrafiltration membrane treatment that the liquid after filtering is adsorbed passes through ultrafiltration system；The nearly saturation strong brine or receive the old halogen after salt that raw material beach obtains after evaporating brine in the step 1.
- A kind of 2. preparation method of flotation fluid according to claim 1, it is characterised in that：Flocculant in the step 1 It is preferably FeCl for Ferric Salt Flocculants or aluminum salt flocculant3Or FeSO4Flocculant.
- A kind of 3. preparation method of flotation fluid according to claim 1, it is characterised in that：Activated carbon in the step 2 Activated carbon in filtration system is cylindrical particulate, and granularity is 0.4~2.5mm, and specific surface area is 450~1500m2/ g, carefully Hole total measurement (volume) is 0.57~1.15m3/g。
- A kind of 4. preparation method of flotation fluid according to claim 1, it is characterised in that：Ultrafiltration membrane in the step 3 Aperture be 0.001~0.01 μm, operating pressure is 0.05MPa~0.1MPa.
- 5. one kind floating liquid preparing system, it is characterised in that：Including the following device being sequentially communicated：Flocculation sedimentation tank, for raw material flocculation treatment；Sedimentation basin, for the particle produced after flocculation treatment to be settled and separated；Active carbon filtering device, for adsorbing contaminant and heavy metal,Ultrafiltration apparatus, for retaining suspended matter and solid impurity.
- A kind of 6. flotation fluid purification method, it is characterised in that：Include the following steps：Step S1, microfiltration process, the flotation fluid after use are handled by microfiltration systems；Step S2, filter process, the flotation fluid after micro-filtration processing are handled by activated carbon filtration system；Step S3, disinfecting process, the flotation fluid after the processing of activated carbon filtration system are carried out disinfection by chlorination equipment.
- 7. one kind floating liquid purification system, it is characterised in that：Including the following device being sequentially communicated：Micro-filtration, for carrying out micro-filtration processing to the flotation fluid after use；Active carbon filtering device, for decolourizing to flotation fluid；Chlorination equipment, for carrying out disinfection to flotation fluid.
- A kind of 8. floating liquid purification system according to claim 7, it is characterised in that：The chlorination equipment is ozonization Device.
- A kind of 9. floating liquid purification system according to claim 7, it is characterised in that：The active carbon filtering device includes：The adsorbent at top adds mouth and flotation fluid entrance；It is internally provided with cleaning position, the cleaning position periphery and the active carbon filtering device elastic connection；In the cleaning position Portion is equipped with filter plate, its two bottom sides is equipped with vibrating motor, its bottom centre exports equipped with flotation fluid, and the flotation fluid outlet is worn The hole for crossing the active carbon filtering device bottom extends downwardly；Preferably, annular sterilizing viltalight lamp is equipped with below the filter plate；Preferably, the adsorbent adds below mouth and flotation fluid inlet port and is equipped with water conservancy diversion inclined-plane, and the water conservancy diversion surface bottom leads to The first elastic hose is crossed with being connected at the top of the cleaning position；Preferably, the flotation fluid outlet tip is connected by the second elastic hose with the cleaning position, its bottom is extended The position of the active carbon filtering device is radially vertically equipped with baffle, and the baffle upper surface is equipped with cushioning piece；Preferably, the cleaning position periphery is connected by multiple metal bracelets with the active carbon filtering device inner wall, the gold The length for belonging to chain is longer than the distance of the cleaning position outer wall and the active carbon filtering device inner wall.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711467008.9A CN107986506A (en) | 2017-12-28 | 2017-12-28 | A kind of preparation method of flotation fluid, preparation system, purification method and cleaning system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711467008.9A CN107986506A (en) | 2017-12-28 | 2017-12-28 | A kind of preparation method of flotation fluid, preparation system, purification method and cleaning system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107986506A true CN107986506A (en) | 2018-05-04 |
Family
ID=62043326
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711467008.9A Pending CN107986506A (en) | 2017-12-28 | 2017-12-28 | A kind of preparation method of flotation fluid, preparation system, purification method and cleaning system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107986506A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110065957A (en) * | 2018-09-29 | 2019-07-30 | 内蒙古博源工程有限责任公司 | A kind of deep refining system of complexity brine |
| CN111807563A (en) * | 2020-08-03 | 2020-10-23 | 许海超 | Industrial sewage purification device |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1704354A (en) * | 2004-06-04 | 2005-12-07 | 天津科技大学 | Floating crystal and floating liquid preparing method |
| CN1772645A (en) * | 2005-09-23 | 2006-05-17 | 成都死海盐疗健康馆服务有限公司 | Prepn of dead sea floated rock salt solution |
| CN1772646A (en) * | 2005-09-23 | 2006-05-17 | 成都死海盐疗健康馆服务有限公司 | Prepn of health floated well salt solution |
| CN1948179A (en) * | 2006-08-30 | 2007-04-18 | 成都死海盐疗健康馆服务有限公司 | Purification treatment method of imitation dead sea floating solution |
| CN202988794U (en) * | 2012-12-25 | 2013-06-12 | 范丽珍 | Air and water purifier using activated carbons |
| CN103880212A (en) * | 2014-03-20 | 2014-06-25 | 苏州腾纳环保科技有限公司 | Vibration type high-efficiency water purification filter element |
-
2017
- 2017-12-28 CN CN201711467008.9A patent/CN107986506A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1704354A (en) * | 2004-06-04 | 2005-12-07 | 天津科技大学 | Floating crystal and floating liquid preparing method |
| CN1772645A (en) * | 2005-09-23 | 2006-05-17 | 成都死海盐疗健康馆服务有限公司 | Prepn of dead sea floated rock salt solution |
| CN1772646A (en) * | 2005-09-23 | 2006-05-17 | 成都死海盐疗健康馆服务有限公司 | Prepn of health floated well salt solution |
| CN1948179A (en) * | 2006-08-30 | 2007-04-18 | 成都死海盐疗健康馆服务有限公司 | Purification treatment method of imitation dead sea floating solution |
| CN202988794U (en) * | 2012-12-25 | 2013-06-12 | 范丽珍 | Air and water purifier using activated carbons |
| CN103880212A (en) * | 2014-03-20 | 2014-06-25 | 苏州腾纳环保科技有限公司 | Vibration type high-efficiency water purification filter element |
Non-Patent Citations (1)
| Title |
|---|
| 民盟天津市委经济科技委员会: "以海水淡化为龙头带动相关产业发展", 《海洋经济》 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110065957A (en) * | 2018-09-29 | 2019-07-30 | 内蒙古博源工程有限责任公司 | A kind of deep refining system of complexity brine |
| CN111807563A (en) * | 2020-08-03 | 2020-10-23 | 许海超 | Industrial sewage purification device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105884086A (en) | Seawater mineral substance and trace element concentrated solution and preparation method and application thereof | |
| CN104085956B (en) | A kind of preparation method of ocean nanofiltration concentrate | |
| CN107158032A (en) | The technique that Essence prepares flotation fluid simultaneously in a kind of extraction seawater | |
| CN107986506A (en) | A kind of preparation method of flotation fluid, preparation system, purification method and cleaning system | |
| Singh et al. | Heavy metal water pollution: an overview about remediation, removal and recovery of metals from contaminated water | |
| CN102452758A (en) | Production process flow of low hertz (HZ) water | |
| CN104150660A (en) | Micro cluster mineral water and preparation method thereof | |
| CN102974319A (en) | Drinking water cleaning agent with arsenic-removal function and preparation method thereof | |
| CN102583868B (en) | Energy filter element tube with information memory | |
| CN201899046U (en) | Travel mug for manufacturing water by net mineralization and micro electrolysis | |
| CN102139988A (en) | Production method for plant enzyme healthy water and equipment thereof | |
| CN105967432A (en) | Preparation method of rare-earth hydrogen-energy water | |
| CN106315941A (en) | Technology for preparing water rich in hydrogen at normal temperature with soft water as base material | |
| CN105858775B (en) | A method of utilizing cobalt in iron aluminium mud efficient absorption water body | |
| CN204897598U (en) | Automatic change multi -functional ultrapure water processing system | |
| CN209178151U (en) | A kind of portable water purifier | |
| CN207061921U (en) | DMI and activated carbon multiple-hearth deep purifying production drinking water device | |
| CN2454373Y (en) | Clean-water treatment | |
| CN205773835U (en) | A kind of Multifunction drinking water purification equipment | |
| CN205892941U (en) | High -efficient emergent safe water treatment facility | |
| CN102603304B (en) | Composite memory material and manufacture method thereof | |
| CN202116400U (en) | Energy filter element tube with information memory function | |
| TWM625514U (en) | Hydrogen-rich ionized water manufacturing equipment for promoting metabolism | |
| CN202625959U (en) | Multifunctional drinking water purifying device | |
| CN208934481U (en) | Floating pool liquid-supplying system and room for user lying |
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: 20180504 |
|
| WD01 | Invention patent application deemed withdrawn after publication |