CN107352704A - A kind of printing ink wastewater recycling device - Google Patents
A kind of printing ink wastewater recycling device Download PDFInfo
- Publication number
- CN107352704A CN107352704A CN201710738442.XA CN201710738442A CN107352704A CN 107352704 A CN107352704 A CN 107352704A CN 201710738442 A CN201710738442 A CN 201710738442A CN 107352704 A CN107352704 A CN 107352704A
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- China
- Prior art keywords
- sewage collecting
- collecting bucket
- printing ink
- pump
- bucket
- 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.)
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- 239000002351 wastewater Substances 0.000 title claims abstract description 39
- 238000007639 printing Methods 0.000 title claims abstract description 25
- 238000004064 recycling Methods 0.000 title claims abstract description 19
- 239000010865 sewage Substances 0.000 claims abstract description 52
- 239000012528 membrane Substances 0.000 claims abstract description 38
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 38
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 34
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 20
- 239000003792 electrolyte Substances 0.000 claims abstract description 20
- 238000010979 pH adjustment Methods 0.000 claims abstract description 17
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 16
- 238000009298 carbon filtering Methods 0.000 claims abstract description 13
- 239000000919 ceramic Substances 0.000 claims abstract description 11
- 239000007788 liquid Substances 0.000 claims description 9
- 229910052751 metal Inorganic materials 0.000 claims description 9
- 239000002184 metal Substances 0.000 claims description 9
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 8
- 230000037452 priming Effects 0.000 claims description 8
- 239000004925 Acrylic resin Substances 0.000 claims description 7
- 229920000178 Acrylic resin Polymers 0.000 claims description 7
- 238000005374 membrane filtration Methods 0.000 claims description 7
- 238000001914 filtration Methods 0.000 claims description 6
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 5
- RSWGJHLUYNHPMX-UHFFFAOYSA-N Abietic-Saeure Natural products C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 claims description 4
- 102100024739 E3 ubiquitin-protein ligase UHRF1 Human genes 0.000 claims description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 4
- 101100483728 Homo sapiens UHRF1 gene Proteins 0.000 claims description 4
- KHPCPRHQVVSZAH-HUOMCSJISA-N Rosin Natural products O(C/C=C/c1ccccc1)[C@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 KHPCPRHQVVSZAH-HUOMCSJISA-N 0.000 claims description 4
- 239000002518 antifoaming agent Substances 0.000 claims description 4
- 229910052742 iron Inorganic materials 0.000 claims description 4
- 239000000049 pigment Substances 0.000 claims description 4
- 239000011148 porous material Substances 0.000 claims description 4
- 239000003381 stabilizer Substances 0.000 claims description 4
- KHPCPRHQVVSZAH-UHFFFAOYSA-N trans-cinnamyl beta-D-glucopyranoside Natural products OC1C(O)C(O)C(CO)OC1OCC=CC1=CC=CC=C1 KHPCPRHQVVSZAH-UHFFFAOYSA-N 0.000 claims description 4
- 235000021419 vinegar Nutrition 0.000 claims description 4
- 239000000052 vinegar Substances 0.000 claims description 4
- 229910052573 porcelain Inorganic materials 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 8
- 239000004480 active ingredient Substances 0.000 abstract description 4
- 230000000694 effects Effects 0.000 description 8
- 239000000463 material Substances 0.000 description 8
- 239000002253 acid Substances 0.000 description 7
- 239000007787 solid Substances 0.000 description 6
- 239000002585 base Substances 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 5
- 238000012545 processing Methods 0.000 description 5
- 230000008859 change Effects 0.000 description 4
- 230000007613 environmental effect Effects 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 230000009286 beneficial effect Effects 0.000 description 3
- 239000003610 charcoal Substances 0.000 description 3
- 239000000084 colloidal system Substances 0.000 description 3
- 239000000645 desinfectant Substances 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- 239000005416 organic matter Substances 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- 239000002910 solid waste Substances 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000000845 anti-microbial effect Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000000701 coagulant Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005189 flocculation Methods 0.000 description 2
- 230000016615 flocculation Effects 0.000 description 2
- 230000004907 flux Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000000499 gel Substances 0.000 description 2
- 239000002920 hazardous waste Substances 0.000 description 2
- 238000001764 infiltration Methods 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 235000014413 iron hydroxide Nutrition 0.000 description 2
- NCNCGGDMXMBVIA-UHFFFAOYSA-L iron(ii) hydroxide Chemical compound [OH-].[OH-].[Fe+2] NCNCGGDMXMBVIA-UHFFFAOYSA-L 0.000 description 2
- 229910000000 metal hydroxide Inorganic materials 0.000 description 2
- 150000004692 metal hydroxides Chemical class 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 238000001223 reverse osmosis Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 238000006467 substitution reaction Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 241000883990 Flabellum Species 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 240000002853 Nelumbo nucifera Species 0.000 description 1
- 235000006508 Nelumbo nucifera Nutrition 0.000 description 1
- 235000006510 Nelumbo pentapetala Nutrition 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 1
- 229910021502 aluminium hydroxide Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- QHIWVLPBUQWDMQ-UHFFFAOYSA-N butyl prop-2-enoate;methyl 2-methylprop-2-enoate;prop-2-enoic acid Chemical compound OC(=O)C=C.COC(=O)C(C)=C.CCCCOC(=O)C=C QHIWVLPBUQWDMQ-UHFFFAOYSA-N 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 125000001309 chloro group Chemical group Cl* 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 230000007717 exclusion Effects 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 231100001240 inorganic pollutant Toxicity 0.000 description 1
- 235000015110 jellies Nutrition 0.000 description 1
- 239000008274 jelly Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 230000001473 noxious effect Effects 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000033116 oxidation-reduction process Effects 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 238000010517 secondary reaction Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 230000010148 water-pollination Effects 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
-
- 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
- C02F1/44—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
- C02F1/444—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
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/465—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electroflotation
-
- 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
- C02F1/467—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
-
- 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
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
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 Electricity Or Magnetism (AREA)
- Water Treatment By Sorption (AREA)
Abstract
The invention discloses a kind of printing ink wastewater recycling device,One end of device body is provided with electrolyte tank,One end of electrolyte tank is provided with system host,The side of electrolyte tank and system host is provided with fixed mount,The inside of fixed mount is provided with sewage collecting bucket,Sewage collecting bucket is provided with mixer,One end of sewage collecting bucket is provided with PH adjustment buckets,One end of PH adjustment buckets is provided with activated carbon filtering tank,Permeable membrane device is divided in one end of activated carbon filtering tank provided with ultrafiltration,PH adjusts bucket and the side of sewage collecting bucket is equipped with filter press,The bottom of device body is provided with base,The inside of electrolyte tank is provided with film bothrium and electrolysis unit,The inside of electrolysis unit is provided with hollow nano ceramic membrane,Structure of the present invention is novel,It is easy to operate,The present apparatus uses brand-new technique,The active ingredient of printing ink wastewater is reclaimed,Its reclaimed water carries out advanced treating Posterior circle use again,Active ingredient in ink can be returned to further in the use link of user by professional's debugging,Just realize zero-emission.
Description
Technical field
The present invention relates to Sewage treatment reuse means, and in particular to a kind of printing ink wastewater recycling device.
Background technology
At present, environmentally friendly water treatment field, the printing machine of printing industry need periodic cleaning, can be produced during cleaning
A large amount of waste water, it has, and colourity is high, turbidity is big, basicity is high, COD is high, bio-refractory, and with substantial amounts of inorganic salts ingredients,
Noxious material, and water quality, water change greatly the features such as, serious pollution is easily caused to water environment, is that taboo is give stricted orders by environmental administration
The industrial wastewater only discharged.And the pollution control of the sector just starts at present.The technique of comparative maturity is oxidation, taken off at present
Color and flocculation sediment+plate compression technique, all it is being relevant device based on this technique on the market.But in processing procedure
In discharge water quality cannot effectively control, particularly produce substantial amounts of solid hazardous waste.Money is needed also exist for
The unit of matter is burned or landfill stabilization.For small, more, scattered packages printing industry, the difficulty of environmental protection supervision is very big, money of wasting water
Source.
The content of the invention
The technical problem that to solve of the present invention is to overcome existing Sewage treatment reuse means to easily cause water environment
Serious pollution, produce the problem of substantial amounts of solid hazardous waste waste water resource, there is provided a kind of printing ink wastewater recovery is sharp again
Use device.
In order to solve the above-mentioned technical problem, the invention provides following technical scheme：
The invention provides a kind of printing ink wastewater recycling device, one end of described device body is provided with electrolyte tank,
One end of the electrolyte tank is provided with system host, and the side of the electrolyte tank and the system host is provided with fixed mount, described solid
The inside for determining frame is provided with sewage collecting bucket, and the sewage collecting bucket is provided with mixer, and one end of the sewage collecting bucket is provided with
PH adjusts bucket, and one end of the PH adjustment bucket is provided with activated carbon filtering tank, and one end of the activated carbon filtering tank is provided with ultrafiltration point
The side of permeable membrane device, the PH adjustment buckets and the sewage collecting bucket is equipped with filter press, the bottom of described device body
Provided with base, the inside of the electrolyte tank is provided with film bothrium and electrolysis unit, and the inside of the electrolysis unit is provided with hollow nano
Ceramic membrane, the bottom of the base are provided with leg, and the bottom of the filter press is provided with fixed plate.
As a preferred technical solution of the present invention, the top of the sewage collecting bucket and PH adjustment buckets, which is provided with, to be connected
Interface, is provided with bearing frame between the sewage collecting bucket and the mixer, the bearing frame is provided with bearing plate, the stirring
One end of machine is provided with motor, and the other end of the mixer is provided with rotary shaft, and the rotary shaft is provided with paddle.
As a preferred technical solution of the present invention, the sewage collecting bucket passes through the external client's ink sewage of self priming pump
Pond, the sewage collecting bucket connect the filter press by membrane pump, and filter press PH as described in connecting tube adjusts bucket, described
PH adjusts bucket and connects the electrolysis unit and the film bothrium by shifting pump, and the film bothrium connects activated carbon by membrane filtration pump
Filtering tank, the activated carbon filtering tank connect the ultrafiltration by the connecting tube and divide permeable membrane device, the sewage collecting bucket
Connected between the electrolyte tank by return pump.
As a preferred technical solution of the present invention, the inside of the electrolysis unit is provided with metal anode and metal is cloudy
Pole, the membrane pump, the membrane filtration pump, the return pump, the shifting pump and the self priming pump are connected by pneumatic three suction parts
Source of the gas.
As a preferred technical solution of the present invention, the hollow nano ceramic membrane is 0.1um by aperture, described
Ultrafiltration, which divides in permeable membrane device, is provided with milipore filter, and the milipore filter is that a kind of aperture specification is consistent, nominal pore for 0.01um with
Under micropore filtering film.
As a preferred technical solution of the present invention, the filter press is plate and frame filter press.
As a preferred technical solution of the present invention, ink modulating liquid, the ink are equipped with inside the PH adjustment bucket
The formula rate of modulating liquid is that rosin content is 25%, pigment content 15%, and acrylic resin content is 35%, industrial alcohol
Content is 6%, and wear-resistant vinegar content is 5%, and antifoam content 2%, stabilizer NP95 contents are 2% and the content of water is 10%
As a preferred technical solution of the present invention, the inside of the electrolysis unit is provided with metal anode and metal is cloudy
Pole.
The beneficial effect that is reached of the present invention is：Structure of the present invention is novel, easy to operate, and the present apparatus uses brand-new work
Skill, the active ingredient of printing ink wastewater is reclaimed, its reclaimed water carries out advanced treating Posterior circle use again, in ink it is effective into
Lease making is crossed professional's debugging and can further returned in the use link of user, just realizes zero-emission, greatly reduces enterprise
Industry handles the cost of waste water and solid waste, while is easy to carry out purification recycling to the waste water of cleaning equipment, so as to save water money
Source, effectively protect environment.
Brief description of the drawings
Accompanying drawing is used for providing a further understanding of the present invention, and a part for constitution instruction, the reality with the present invention
Apply example to be used to explain the present invention together, be not construed as limiting the invention.In the accompanying drawings：
Fig. 1 is the agent structure schematic diagram of the present invention；
Fig. 2 is the workflow structure schematic diagram of the present invention；
Fig. 3 is the equipment cleaning process flow structural representation of the present invention；
In figure：1st, device body；2nd, electrolyte tank；3rd, filter press；4th, mixer；5th, activated carbon filtering tank；6th, ultrafiltration point is oozed
Permeable membrane device；7th, fixed mount；8th, PH adjusting tanks；9th, sewage collecting bucket；10th, base；11st, system host；12nd, membrane pump；13rd, it is electric
Solve device；14th, shifting pump；15th, pneumatic three inhale part；16th, membrane filtration pump；17th, film bothrium；18th, pump is returned；19th, PH adjustment tanks；20、
Self priming pump；21st, hollow nano ceramic membrane.
Embodiment
The preferred embodiments of the present invention are illustrated below in conjunction with accompanying drawing, it will be appreciated that described herein preferred real
Apply example to be merely to illustrate and explain the present invention, be not intended to limit the present invention.
Embodiment 1
As Fig. 1-3 shows, the invention provides a kind of printing ink wastewater recycling device, one end of device body 1 is provided with
Electrolyte tank 2, one end of electrolyte tank 2 are provided with system host 11, and the side of electrolyte tank 2 and system host 11 is provided with fixed mount 7, Gu
The inside for determining frame 7 is provided with sewage collecting bucket 9, and sewage collecting bucket 9 is provided with mixer 4, and one end of sewage collecting bucket 9 is adjusted provided with PH
Whole bucket 8, one end of PH adjustment buckets 8 are provided with activated carbon filtering tank 5, and one end of activated carbon filtering tank 5 divides permeable membrane to fill provided with ultrafiltration
The side for putting 6, PH adjustment buckets 8 and sewage collecting bucket 9 is equipped with filter press 3, and the bottom of device body 1 is provided with base 10, electrolysis
The inside of case 2 is provided with film bothrium 17 and electrolysis unit 13, and the inside of electrolysis unit 13 is provided with hollow nano ceramic membrane 21, base 10
Bottom be provided with leg, the bottom of filter press 3 is provided with fixed plate.
The top of sewage collecting bucket 9 and PH adjustment buckets 8 is provided with connector, the transfer being easy between sewage, sewage collecting bucket 9
Bearing frame is provided between mixer 4, bearing frame is provided with bearing plate, is easy to fixed drive motor, so as to which mixer 4 be consolidated
It is scheduled in sewage collecting bucket 9, one end of mixer 4 is provided with motor, and the other end of mixer is provided with rotary shaft, in rotary shaft
Provided with paddle, it is easy to stir ink sewage.
Sewage collecting bucket 9 is connected by the external client's ink cesspool of self priming pump 20, sewage collecting bucket 9 by membrane pump 12
Filter press 3, filter press 3 adjust bucket 8 by connecting tube PH, and PH adjusts bucket 8 and connects electrolysis unit 13 and film bothrium by shifting pump 14
17, film bothrium 17 connects activated carbon filtering tank 5 by membrane filtration pump 16, and activated carbon filtering tank 5 connects ultrafiltration point by connecting tube and oozed
Permeable membrane device 6, connected between sewage collecting bucket 9 and electrolyte tank 2 by return pump 18, the transmission being easy between ink sewage, favorably
Reused in sewage recycling and by residue progress ink readjustment.
The inside of electrolysis unit 13 is provided with metal anode and metallic cathode, is easy to sewage carrying out electrolysis processing, is advantageous to
Sewage purification is carried out, membrane pump 12, membrane filtration pump 16, return pump 18, shifting pump 14 and self priming pump 20 are connected by pneumatic three suction parts 15
Source of the gas is connect, is easy to provide the power between air pump.
Hollow nano ceramic membrane 21 is 0.1um by aperture, and ceramic membrane is 0.1um by aperture, is further removed
The molecule and floccule of formation are electrolysed in waste water, because inorganic flat ceramic membrane contrast conventional film has clear advantage：
1st, efficiently：Membrane flux improves 3-4 times on the basis of conventional film, and filter area is big；2nd, anti-soil：Acid and alkali-resistance, organic solvent-resistant,
Resistance to bacterium, antimicrobial, antipollution；3rd, heat resistance is good；4th, aperture is adjustable at 10 nanometers -10 microns；5th, go out in entering outside category, no
Easily block；6th, can air purge, washing or soda acid wash, ultrafiltration, which divides in permeable membrane device 6, is provided with milipore filter, and milipore filter is a kind of bore gauge
Lattice are consistent, and nominal pore is below 0.01um micropore filtering film, and ultrafiltration point permeable membrane device 6 can not pass through according to other materials
Pellicle and these materials and water are separated.The membrane aperture of reverse osmosis membrane is very small, therefore can effectively go in water removal
Dissolved salts, colloid, microorganism, organic matter etc..
Filter press 3 is plate and frame filter press, is convenient for separation of solid and liquid.
Ink modulating liquid is equipped with inside PH adjustment buckets 8, the formula rate of ink modulating liquid is that rosin content is 25%, pigment
Content is 15%, and acrylic resin content is 35%, and industrial alcohol content is 6%, and wear-resistant vinegar content is 5%, antifoam content
For 2%, stabilizer NP95 contents are 2% and the content of water is 10%, and and can is dissolved in rapidly water after the PH for the residue for being easy to change
In.
Metal anode and metallic cathode are made using iron or aluminum metal, the ion dissolved due to iron or aluminum metal anode
Further hydrolysis, can generate the metal hydroxides activity coagulant not soluble in water such as iron hydroxide or aluminium hydroxide, this
Material has porous gel structure, has surface charge effect and stronger suction-operated.
During specific work, the sewage that client's ink sewage and equipment clean is pumped into sewage collecting bucket by self priming pump 20 first
9, disinfectant is added in sewage collecting bucket 9, in water-based ink, containing a large amount of acrylic resins, acrylic resin not only has
There is stronger hydrophily, and it is higher to PH susceptibility.Therefore neutralization reaction is carried out using acid, since it is considered that strong acid is strong
Alkali is management and control material, and we are that NaCLO pulvis is added in printing ink wastewater using disinfectant common on the market, and regulation pH value arrives
Between 5.0-5.5, in the case where waste water is in acid state, the jelly in waste water largely separates out, and wherein ink powder is in particulate, by
Step is separated from the water out, rear stirrer 4 rotary shaft is rotated by motor, rotary shaft Stirring flabellum enters to sewage
Row stirring, makes disinfectant play one's part to the full, and sewage is pumped into filter press 3 by membrane pump 12 afterwards, the master in printing ink wastewater
After a large amount of precipitations for wanting the binders such as composition and acrylic resin, by the separation of solid and liquid of filter press 3, substantial amounts of clear water is formed
And the scoriform thing being made up of ink main component.Clear water and scoriform thing enter next link and further handled, and are adjusted in PH
The pH value of ink sewage is detected in case 8 first, afterwards by adjusting the scoriform thing of PH precipitations, and can is fast after its PH of change
Be instantly dissolved in water, thus further according to ink modulation ratio with scoriform thing further can be modulated into new ink can be secondary
Utilize, have multiple color during user uses ink, but we are by testing and using drawing a conclusion, multiple color
Printing ink wastewater mix after all become black, so readjustment all black of ink, ink modulation formula rate
Usually rosin content is 25%, pigment content 15%, and acrylic resin content is 35%, and industrial alcohol content is 6%, is resisted
It is 5% to grind vinegar content, and antifoam content 2%, stabilizer NP95 contents are 2% and the content of water is 10%, in PH adjustment tanks
The formula of ink modulation is added in 19, sewage is transferred in electrolyte tank 2 by shifting pump 14 afterwards, and electrolysis unit 13 passes through afterwards
Metal anode and metallic cathode carry out primary reaction and secondary reaction processing waste water effect is outer, the also effect because of electrolysis water, point
Hydrogen and oxygen are not produced in negative electrode and anode, (H) and (0) of both nascent platforms can play chemistry to the pollutant in waste water
Reduction and the effect of oxidation, and tiny rill can be produced, flocculate and grease is attached to bubble floating to liquid level respectively has
Beneficial to exclusion.Further, since iron or the ion of aluminum metal anode dissolving further hydrolyze, iron hydroxide or hydrogen-oxygen can be generated
Changing metal hydroxides activity coagulant not soluble in water, this materials such as aluminium has porous gel structure, has surface electricity
Lotus acts on and stronger suction-operated, obvolvent cohesion can be played to the organic or inorganic pollutant in waste water, so that pollution
Thing phase inter coagulation is separated from waste water.Here it is electric flotation and electrolytic flocculation to be handled.Acted on, broken by electrolysis oxidation-reduction
Bad chromophore, so as to obtain good decolorizing effect.The colourity and COD in waste water are greatly reduced, sewage is by receiving afterwards
Rice hollow ceramic membranes 21 are 0.1um by aperture, further remove the molecule and floccule that formation is electrolysed in waste water, by
There is clear advantage in inorganic flat ceramic membrane contrast conventional film：1st, efficiently：Membrane flux improves on the basis of conventional film
3-4 times, filter area is big；2nd, anti-soil：Acid and alkali-resistance, organic solvent-resistant, resistance to bacterium, antimicrobial, antipollution；3rd, heat resistance is good；
4th, aperture is adjustable at 10 nanometers -10 microns；5th, go out in entering outside category, be not easily blocked；6th, can air purge, washing or soda acid wash, live afterwards
Property charcoal filtering tank 5 using the porous property of activated carbon, one or more harmful substances in water is attracted to the surface of solids and is gone
The method removed.Charcoal absorption is for going organic matter, colloid, microorganism, chlorine residue, peculiar smell etc. in water removal to have good effect
Fruit.Activated carbon also has certain reduction simultaneously, therefore the oxidant that also can effectively go in water removal.Made pottery from hollow nano
Water after porcelain film 21 filters can meet three class discharge standards or recycling, it is necessary to further improve water after charcoal absorption
Matter, secondary filter and the salinity gone by reverse osmosis unit in water removal, ultrafiltration afterwards point infiltration further can be carried out by ultrafiltration
Milipore filter is provided with film device 6, milipore filter is that a kind of aperture specification is consistent, and nominal pore is below 0.01um micro porous filtration
Film, ultrafiltration point permeable membrane device 6 can not pass through pellicle according to other materials and separate these materials and water, counter-infiltration
The membrane aperture of film is very small, therefore dissolved salts, colloid, microorganism, the organic matter etc. that can effectively go in water removal, so as to reach
Qualified discharge or recycling after to ink sewage disposal；Saving water resource, environmental protection, printing ink wastewater residue are turned waste into wealth,
Secondary use, no solid waste discharge, economizes on resources, environmental protection.Use low-voltage dc power supply, it is not necessary to a large amount of chemical agent consumptions；
Operate at normal temperatures and pressures, management is easy, such as change in concentration in waste water, can ensure by the method for adjusting voltage x current
Water is stable, and processing unit floor space is small.Small wastewater flow rate processing is especially suitable for, the water of the purification of permeable membrane device 6 is divided by ultrafiltration
Discharged or recycled.
The beneficial effect that is reached of the present invention is：Structure of the present invention is novel, easy to operate, and the present apparatus uses brand-new work
Skill, the active ingredient of printing ink wastewater is reclaimed, its reclaimed water carries out advanced treating Posterior circle use again, in ink it is effective into
Lease making is crossed professional's debugging and can further returned in the use link of user, just realizes zero-emission, greatly reduces enterprise
Industry handles the cost of waste water and solid waste, while is easy to carry out purification recycling to the waste water of cleaning equipment, so as to save water money
Source, effectively protect environment.
Finally it should be noted that：The preferred embodiment of present invention described above, is not intended to limit the invention, although
The present invention is described in detail with reference to the foregoing embodiments, for those skilled in the art, it still can be right
Technical scheme described in foregoing embodiments is modified, or carries out equivalent substitution to which part technical characteristic.It is all
Within the spirit and principles in the present invention, any modification, equivalent substitution and improvements made etc., the protection of the present invention should be included in
Within the scope of.
Claims (8)
1. a kind of printing ink wastewater recycling device, including device body (1), it is characterised in that described device body (1)
One end is provided with electrolyte tank (2), and one end of the electrolyte tank (2) is provided with system host (11), the electrolyte tank (2) and the system
The side of main frame (11) is provided with fixed mount (7), and the inside of the fixed mount (7) is provided with sewage collecting bucket (9), the sewage collecting
Bucket (9) is provided with mixer (4), and one end of the sewage collecting bucket (9) is provided with PH adjustment buckets (8), the PH adjustment buckets (8)
One end is provided with activated carbon filtering tank (5), and permeable membrane device (6) is divided in one end of the activated carbon filtering tank (5) provided with ultrafiltration, described
The side of PH adjustment buckets (8) and the sewage collecting bucket (9) is equipped with filter press (3), and the bottom of described device body (1) is provided with
Base (10), the inside of the electrolyte tank (2) are provided with film bothrium (17) and electrolysis unit (13), the electrolysis unit (13) it is interior
Portion is provided with hollow nano ceramic membrane (21), and the bottom of the base (10) is provided with leg, and the bottom of the filter press (3) is provided with admittedly
Fixed board.
A kind of 2. printing ink wastewater recycling device according to claim 1, it is characterised in that the sewage collecting bucket
(9) and the PH adjustment bucket (8) top be provided with connector, be provided between the sewage collecting bucket (9) and the mixer (4)
Bearing frame, the bearing frame are provided with bearing plate, and one end of the mixer (4) is provided with motor, the mixer it is another
One end is provided with rotary shaft, and the rotary shaft is provided with paddle.
A kind of 3. printing ink wastewater recycling device according to claim 1, it is characterised in that the sewage collecting bucket
(9) pressure is connected by membrane pump (12) by the external client's ink cesspool of self priming pump (20), the sewage collecting bucket (9)
Filter (3), the filter press (3) PH as described in connecting tube adjust bucket (8), and the PH adjustment buckets (8) are connected by shifting pump (14)
The electrolysis unit (13) and the film bothrium (17) are connect, the film bothrium (17) connects activated carbon by membrane filtration pump (16) and filtered
Tank (5), the activated carbon filtering tank (5) connect the ultrafiltration by the connecting tube and divide permeable membrane device (6), and the sewage is received
Collect and connected between bucket (9) and the electrolyte tank (2) by return pump (18).
A kind of 4. printing ink wastewater recycling device according to claim 3, it is characterised in that the electrolysis unit
(13) inside is provided with metal anode and metallic cathode, the membrane pump (12), the membrane filtration pump (16), the return pump
(18), the shifting pump (14) and the self priming pump (20) inhale part (15) connection source of the gas by pneumatic three.
A kind of 5. printing ink wastewater recycling device according to claim 1, it is characterised in that the hollow nano pottery
Porcelain film (21) is 0.1um by aperture, and the ultrafiltration, which divides in permeable membrane device (6), is provided with milipore filter, and the milipore filter is one
Kind aperture specification is consistent, and nominal pore is below 0.01um micropore filtering film.
A kind of 6. printing ink wastewater recycling device according to claim 1, it is characterised in that the filter press (3)
For plate and frame filter press.
7. a kind of printing ink wastewater recycling device according to claim 1, it is characterised in that the PH adjusts bucket
(8) internal to be equipped with ink modulating liquid, the formula rate of the ink modulating liquid is that rosin content is 25%, and pigment content is
15%, acrylic resin content is 35%, and industrial alcohol content is 6%, and wear-resistant vinegar content is 5%, antifoam content 2%,
Stabilizer NP95 contents are 2% and the content of water is 10%.
A kind of 8. printing ink wastewater recycling device according to claim 1, it is characterised in that the metal anode and
Metallic cathode is made using iron or aluminum metal.
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| CN201710738442.XA CN107352704A (en) | 2017-08-18 | 2017-08-18 | A kind of printing ink wastewater recycling device |
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| CN201710738442.XA CN107352704A (en) | 2017-08-18 | 2017-08-18 | A kind of printing ink wastewater recycling device |
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Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000256602A (en) * | 1999-03-05 | 2000-09-19 | Toppan Printing Co Ltd | Printed matter using ink containing regenerated vegetable oil |
| CN101649134A (en) * | 2009-09-18 | 2010-02-17 | 广州市恒远彩印有限公司 | Waste-ink renewable ink and preparation method thereof |
| CN102674633A (en) * | 2012-05-21 | 2012-09-19 | 传美讯电子科技（珠海）有限公司 | Treatment equipment and process for sewage in production process of ink-jet ink |
| CN102911555A (en) * | 2012-10-30 | 2013-02-06 | 蚌埠市比优特包装印务有限责任公司 | Method for producing water-soluble ink for carton printing with abandoned offset printing ink |
| CN103613999A (en) * | 2013-11-28 | 2014-03-05 | 张家港威迪森化学有限公司 | Water-based ink |
| CN103787551A (en) * | 2014-01-26 | 2014-05-14 | 广东威迪科技股份有限公司 | Treatment method of printing ink wastewater generated in circuit board production |
| CN105565553A (en) * | 2015-12-22 | 2016-05-11 | 解艳超 | Zero-emission purifying and recycling system of cyanide-containing heavy metal wastewater |
| CN106315932A (en) * | 2016-08-24 | 2017-01-11 | 厦门世达膜科技有限公司 | Method for disposing wastewater from oil field |
| CN106396211A (en) * | 2016-12-16 | 2017-02-15 | 中国人民解放军后勤工程学院 | Electrocoagulation and ceramic micro-filtration membrane coupling device for purifying micro-polluted source water as well as process |
| CN207330594U (en) * | 2017-08-18 | 2018-05-08 | 沈瑞忠 | A kind of printing ink wastewater recycling device |
-
2017
- 2017-08-18 CN CN201710738442.XA patent/CN107352704A/en active Pending
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000256602A (en) * | 1999-03-05 | 2000-09-19 | Toppan Printing Co Ltd | Printed matter using ink containing regenerated vegetable oil |
| CN101649134A (en) * | 2009-09-18 | 2010-02-17 | 广州市恒远彩印有限公司 | Waste-ink renewable ink and preparation method thereof |
| CN102674633A (en) * | 2012-05-21 | 2012-09-19 | 传美讯电子科技（珠海）有限公司 | Treatment equipment and process for sewage in production process of ink-jet ink |
| CN102911555A (en) * | 2012-10-30 | 2013-02-06 | 蚌埠市比优特包装印务有限责任公司 | Method for producing water-soluble ink for carton printing with abandoned offset printing ink |
| CN103613999A (en) * | 2013-11-28 | 2014-03-05 | 张家港威迪森化学有限公司 | Water-based ink |
| CN103787551A (en) * | 2014-01-26 | 2014-05-14 | 广东威迪科技股份有限公司 | Treatment method of printing ink wastewater generated in circuit board production |
| CN105565553A (en) * | 2015-12-22 | 2016-05-11 | 解艳超 | Zero-emission purifying and recycling system of cyanide-containing heavy metal wastewater |
| CN106315932A (en) * | 2016-08-24 | 2017-01-11 | 厦门世达膜科技有限公司 | Method for disposing wastewater from oil field |
| CN106396211A (en) * | 2016-12-16 | 2017-02-15 | 中国人民解放军后勤工程学院 | Electrocoagulation and ceramic micro-filtration membrane coupling device for purifying micro-polluted source water as well as process |
| CN207330594U (en) * | 2017-08-18 | 2018-05-08 | 沈瑞忠 | A kind of printing ink wastewater recycling device |
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Application publication date: 20171117 |