CN204625822U - A kind of Electroplate liquid filter of exempting from renew cartridge - Google Patents
A kind of Electroplate liquid filter of exempting from renew cartridge Download PDFInfo
- Publication number
- CN204625822U CN204625822U CN201520339624.6U CN201520339624U CN204625822U CN 204625822 U CN204625822 U CN 204625822U CN 201520339624 U CN201520339624 U CN 201520339624U CN 204625822 U CN204625822 U CN 204625822U
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- separation assembly
- membrane separation
- tank
- pipeline
- tubular membrane
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Abstract
The utility model discloses a kind of Electroplate liquid filter of exempting from renew cartridge; It is characterized in that: comprise the plating solution tank be connected with plating tank, described plating solution tank connects recycle pump, tubular membrane separation assembly by pipeline, the dialyzate outlet of described tubular membrane separation assembly connects plating tank by pipeline, also comprise a concentrated flow container, the concentrated solution outlet of described tubular membrane separation assembly connects concentrated flow container by pipeline; Also comprise a cleaning agent tank and a clean water tank, described cleaning agent tank is connected scavenging pump, the liquor inlet of tubular membrane separation assembly and/or the dialyzate outlet of tubular membrane separation assembly with clean water tank by pipeline.Device described in the utility model, carries out electroplate liquid filtration, can free of replacement filter core, there is the advantage that solid waste amount is few, cleaning efficiency is high, effective simultaneously.
Description
Technical field
The utility model relates to electroplate liquid filtration art, particularly a kind of Electroplate liquid filter of exempting from renew cartridge.
Background technology
The filtration of electroplate liquid realized in Japan first in nineteen fifty.Strainer at that time, using porous ceramic tube as filtering element, makes urceolus with the steel applying resistance to acid paint, and with the toothed gear pump as auxiliary facility.Nineteen fifty-five, along with the development of infusion pump and filtration medium technology, have developed radial pre-coating strainer.1967, the filter cartridge type filter for Waste recovery obtains generally to be applied.Develop into now, inside have the strainer of axial disc-type filter core to obtain fairly large application.Filter with pre-coating during dregginess height; Filter with filer element type when dregginess is low.But filter with filer element type and have following shortcoming: when changing, because electroplate liquid has corrodibility and toxicity, personnel need to dress the protective articles such as protective clothing and protective gloves, take longer to change, the protective articles of Clean-mistake of also will taking time after replacing; The occasion of usual replacing is limited space, and outside causing having more than several electroplate liquids to fall when changing secondary containing, result is that secondary is contained exterior domain and polluted; Usually in the place secondary of filter is contained, have solid-plated liquid residue, and small part residue is easily taken out of secondary and is contained outer and pollute and contain external environment region; The occasion that dregginess is high can not be applicable to; Regularly to spend to purchase new filter core and supplement the more stock that causes of renew cartridge and reduce; Not singly that the solid particulate be attached on filter core produces solid slag, also have filter core and the electroplate liquid be attached on filter core to produce solid slag yet, jointly cause changing the not little solid slag produced at every turn.
Summary of the invention
For the problems referred to above, the purpose of this utility model is to provide a kind of free of replacement filter core, good filtration effect, can carry out the Electroplate liquid filter of exempting from renew cartridge of cleaning automatically simultaneously.
For achieving the above object, the technical scheme that the utility model proposes is: a kind of Electroplate liquid filter of exempting from renew cartridge; It is characterized in that: comprise the plating solution tank be connected with plating tank, described plating solution tank connects recycle pump, tubular membrane separation assembly by pipeline, the dialyzate outlet of described tubular membrane separation assembly connects plating tank by pipeline, also comprise a concentrated flow container, the concentrated solution outlet of described tubular membrane separation assembly connects concentrated flow container by pipeline; Also comprise a cleaning agent tank and a clean water tank, described cleaning agent tank is connected scavenging pump, the liquor inlet of tubular membrane separation assembly and/or the dialyzate outlet of tubular membrane separation assembly with clean water tank by pipeline, and the dialyzate outlet of described tubular membrane separation assembly is all provided with pipeline with concentrated solution outlet and is connected with clean water tank with cleaning agent tank; The pipeline that described scavenging pump is connected with tubular membrane separation assembly is connected with a pneumatic jacking-up device.
Further, described scavenging pump is Pneumatic cleaning pump or driven cleaning pump.
Further, the membrane element in described tubular membrane separation assembly is tubular type list core ceramic membrane or tubular type multicore ceramic membrane or tubular type PE film or tubular type plastic film.
Further, described membrane element is inner pressed membrane element.
Further, the film internal diameter of described membrane element is 0.5cm-5cm.
Further, the filter area of described membrane element is 0.1um-0.3um or 1um-3um.
Adopt technique scheme, Electroplate liquid filter of exempting from renew cartridge described in the utility model, adopt tubular membrane separation assembly, carry out electroplate liquid filtration, the beneficial effect had is:
1) the free of replacement time;
2) filter core consumptive material expense is exempted from;
3) avoid potential personal injury because of electroplate liquid tool corrodibility and toxicity, maintenance personnel has the potential risk that comes to harm at replacing maintenance room, and adopts this device to exempt from renew cartridge, then avoid potential personal injury;
4) multiple cleaning way combination, effectively improves cleaning efficiency and cleaning performance;
5) avoid feed liquid and solid slag to pollute secondary and contain outer region;
6) solid waste amount is few.
Accompanying drawing explanation
Fig. 1 is Electroplate liquid filter schematic diagram 1 of exempting from renew cartridge described in the utility model;
Fig. 2 is Electroplate liquid filter schematic diagram 2 of exempting from renew cartridge described in the utility model;
Fig. 3 is Electroplate liquid filter schematic diagram 3 of exempting from renew cartridge described in the utility model.
Embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is described further.
The Electroplate liquid filter embodiment one exempting from renew cartridge described in the utility model; As shown in Figure 1, comprise the plating solution tank 11 be connected with plating tank 10, described plating solution tank 11 connects recycle pump 12, tubular membrane separation assembly 13 by pipeline, the dialyzate outlet of described tubular membrane separation assembly 13 connects plating tank 10 by pipeline, also comprise a concentrated flow container 18, the concentrated solution outlet of described tubular membrane separation assembly 13 connects concentrated flow container 18 by pipeline; Also comprise cleaning agent tank 14 and a clean water tank 15, described cleaning agent tank 14 is connected Pneumatic cleaning pump 16, the liquor inlet of tubular membrane separation assembly and the dialyzate outlet of tubular membrane separation assembly with clean water tank 15 by pipeline, simultaneously scavenging pump and tubular membrane separation assembly dialyzate export on the pipeline that is connected and are connected with a pneumatic jacking-up device 17, adopt in this way can to the membrane element in tubular membrane separation assembly carry out positive/negative to clean water, positive/negatively to clean to medicament and positive/negatively to wash to air water.
The Electroplate liquid filter embodiment two exempting from renew cartridge described in the utility model, as shown in Figure 2, the difference of itself and Fig. 1 is, scavenging pump in Fig. 1 adopts Pneumatic cleaning pump 16, scavenging pump in Fig. 2 adopts driven cleaning pump 19, cleaning agent tank 14 and clean water tank 15 are connected the liquor inlet of driven cleaning pump 19, tubular membrane separation assembly by pipeline simultaneously, can carry out forward clean water, the cleaning of forward medicament and forward air water like this wash the membrane element in tubular membrane separation assembly.
The Electroplate liquid filter embodiment three exempting from renew cartridge described in the utility model, as shown in Figure 3, the difference of itself and Fig. 2 is, cleaning agent tank 14 and clean water tank 15 are connected the dialyzate outlet of driven cleaning pump 19, tubular membrane separation assembly by pipeline, can carry out reverse clean water, oppositely medicament cleaning and reverse air water like this wash the membrane element in tubular membrane separation assembly.
Further, membrane element in described tubular membrane separation assembly is tubular type list core ceramic membrane or tubular type multicore ceramic membrane or tubular type PE film or tubular type plastic film, described membrane element is inner pressed membrane element, and the film internal diameter of described membrane element is 0.5cm-5cm, the filter area of described membrane element is 0.1um-0.3um or 1um-3um.
During concrete use, adopt the filtration process of Electroplate liquid filter described in the utility model, comprise the steps:
Step 1: first by the plating solution in plating solution tank through recycle pump pressurization after, enter in tubular membrane separation assembly and carry out cross flow filter, the dialyzate after filtration enters plating tank, and concentrated solution then enters concentrated flow container;
Step 2: after plating solution liquid level attains to a high place in flow container to be concentrated, carries out the bath filter in concentrated flow container, and the dialyzate after filtration enters plating tank, and concentrated solution then enters concentrated flow container circulating filtration; Until after plating solution liquid level reaches low level in concentrated flow container, carry out the bath filter in plating solution tank;
Step 3: step 1 and step 2 are carried out in circulation;
Step 4: when membrane element need clean in tubular membrane component, carries out Membrane cleaning, first by pneumatic jacking-up device, the plating solution press-in in pipeline is concentrated flow container before cleaning; Then carry out membrane element cleaning, after having cleaned, re-start bath filter in the plating solution tank in step 1.Cleaning way wherein described in step 4 can adopt: medicament forward one or more modes of cleaning in gentle washing in the cleaning of clear water forward in clean water tank, cleaning agent tank hocket (Fig. 2), or clear water reverse cleaning, one or more modes in the gentle washing of medicament reverse cleaning in cleaning agent tank hocket (Fig. 3); Or the cleaning of clear water forward, the cleaning of clear water reverse cleaning, medicament forward, medicament reverse cleaning, forward air water are washed or oppositely air water wash in one or more modes of carrying out alternately cleaning carry out cleaning (Fig. 1).
By adopting said apparatus, carry out electroplate liquid filtration, the beneficial effect had is: exempt from filter core consumptive material expense, avoids more renew cartridge to be simultaneously, potential personal injury; The free of replacement time; Avoid feed liquid and solid slag to pollute secondary and contain outer region; Solid waste amount is few; Adopt multiple cleaning way to combine, effectively improve cleaning efficiency and cleaning performance.
Although specifically show in conjunction with preferred embodiment and describe the utility model; but those skilled in the art should be understood that; not departing from the spirit and scope of the present utility model that appended claims limits; in the form and details the utility model is made a variety of changes, be protection domain of the present utility model.
Claims (4)
1. exempt from the Electroplate liquid filter of renew cartridge for one kind; It is characterized in that: comprise the plating solution tank be connected with plating tank, described plating solution tank connects recycle pump, tubular membrane separation assembly by pipeline, the dialyzate outlet of described tubular membrane separation assembly connects plating tank by pipeline, also comprise a concentrated flow container, the concentrated solution outlet of described tubular membrane separation assembly connects concentrated flow container by pipeline; Also comprise a cleaning agent tank and a clean water tank, described cleaning agent tank is connected scavenging pump, the liquor inlet of tubular membrane separation assembly and/or the dialyzate outlet of tubular membrane separation assembly with clean water tank by pipeline, and the dialyzate outlet of described tubular membrane separation assembly is all provided with pipeline with concentrated solution outlet and is connected with clean water tank with cleaning agent tank; The pipeline that described scavenging pump is connected with tubular membrane separation assembly is connected with a pneumatic jacking-up device.
2. Electroplate liquid filter of exempting from renew cartridge according to claim 1; It is characterized in that: described scavenging pump is Pneumatic cleaning pump or driven cleaning pump.
3. Electroplate liquid filter of exempting from renew cartridge according to claim 1; It is characterized in that: the membrane element in described tubular membrane separation assembly is tubular type list core ceramic membrane, tubular type multicore ceramic membrane or tubular type PE film or tubular type plastic film.
4. Electroplate liquid filter of exempting from renew cartridge according to claim 3; It is characterized in that: described membrane element is inner pressed membrane element.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201520339624.6U CN204625822U (en) | 2015-05-25 | 2015-05-25 | A kind of Electroplate liquid filter of exempting from renew cartridge |
Applications Claiming Priority (1)
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CN201520339624.6U CN204625822U (en) | 2015-05-25 | 2015-05-25 | A kind of Electroplate liquid filter of exempting from renew cartridge |
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CN204625822U true CN204625822U (en) | 2015-09-09 |
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CN201520339624.6U Expired - Fee Related CN204625822U (en) | 2015-05-25 | 2015-05-25 | A kind of Electroplate liquid filter of exempting from renew cartridge |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104846423A (en) * | 2015-05-25 | 2015-08-19 | 威士邦(厦门)环境科技有限公司 | Device and technique for filtering electroplating solution without replacing filter element |
CN105749601A (en) * | 2016-04-28 | 2016-07-13 | 四川昊吉科技有限公司 | Electroplate liquid filtering machine free of replacement of filter bag |
-
2015
- 2015-05-25 CN CN201520339624.6U patent/CN204625822U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104846423A (en) * | 2015-05-25 | 2015-08-19 | 威士邦(厦门)环境科技有限公司 | Device and technique for filtering electroplating solution without replacing filter element |
CN105749601A (en) * | 2016-04-28 | 2016-07-13 | 四川昊吉科技有限公司 | Electroplate liquid filtering machine free of replacement of filter bag |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150909 Termination date: 20180525 |
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CF01 | Termination of patent right due to non-payment of annual fee |