CN108193203A - A kind of application phosphorizing residue removal system - Google Patents
A kind of application phosphorizing residue removal system Download PDFInfo
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- CN108193203A CN108193203A CN201810070990.4A CN201810070990A CN108193203A CN 108193203 A CN108193203 A CN 108193203A CN 201810070990 A CN201810070990 A CN 201810070990A CN 108193203 A CN108193203 A CN 108193203A
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- filter
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C22/00—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C22/86—Regeneration of coating baths
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Abstract
The invention discloses a kind of application phosphorizing residue removal systems, including Phosphating Slot, Phosphating Slot is connect with phosphatization precipitation tank, phosphatization precipitation tank connects several filters of series/parallel by pipeline and the first delivery pump, filter is connect by pipeline and filter pump with phosphatization dope storage bin, phosphatization dope storage bin is connect by pipeline and the second delivery pump with inverse filter, inverse filter is connect by pipeline and third delivery pump with full dose filtering type slag remover, and full dose filtering type slag remover coordinates pipeline to connect anti-cleaning device and/or filtering film component by valve;Anti- cleaning device is also connect, and match and form anti-scavenger circuit by cleaning pipe, cleaning pump and the first valve with the liquid/gas mouth that returns of full dose filtering type slag remover;The clarification phosphating solution of filtering film component and phosphatization precipitation tank, inverse filter from the first liquid outlet of phosphatization precipitation tank, the liquid outlet outflow of the liquid outlet and full dose filtering type slag remover of inverse filter sends Phosphating Slot back to after filter membrane component filters by return pipe.
Description
Technical field
The present invention relates to application techniques field, more particularly to a kind of application phosphorizing residue removal system.
Background technology
For large size industrial enterprise, application and electrophoresis are main production lines, especially for truck, automobile making
Enterprise.For application and electrophoresis production line, it is necessary to satisfaction produces to assemble matched phosphorizing residue removal system.But
Deficiency existing for the phosphorizing residue removal system of some enterprises in existing is:First, effect is poor, pipeline blockage, leakage are tight for slagging-off
Weight, the surface attaching particles so as to cause electrophoresis post-processing part are more, need just to can guarantee the smooth of product surface by polishing,
And processing of polishing can affect the follow-up coating quality of workpiece；Second is that existing plate and frame filter press is backward in technique, and slag,
There are problems that phosphatization slag liquid content is high, equipment leakage in liquid separation process, phosphating solution caused to be lost in serious, so as to cause waste and
Subsequent wastewater treatment cost increases, and phosphating solution dregginess is high, easy blocking pipeline system, reduces sprinkling equipment effect, nothing
Method cleans up the phosphatization slag of workpiece, and also resulting in the attachment of work piece surface phosphatization slag increases, and can cause a large amount of
Phosphatization slag is brought into electrophoresis tank, is influenced the maintenance of electrophoresis groove liquid and is blocked ultrafiltration membrane, increases the later maintenance cost of electrophoresis tank；Three
It is that part phosphorizing residue removal system eliminates phosphatization inclined plate sedimentation system, phosphatization slag in phosphating solution is caused to be not easy to remove.
Invention content
The technical problem to be solved by the present invention is to be directed to defect present in existing design technology, a kind of application phosphatization is provided
Slag removing system, the phosphorizing residue removal system solve the problems, such as pipeline blockage, equipment leakage, improve the utilization rate of phosphating solution, reduce
The maintaining expense of relevant device.
To solve above-mentioned technical problem, the technical solution that the present invention takes is as follows：A kind of application phosphorizing residue removal system, packet
Phosphating Slot is included, the Phosphating Slot is connect by delivery pump with phosphatization precipitation tank, and delivery pump energy will be along Phosphating Slot liquid outlet
The phosphating solution of discharge is sent into the phosphatization precipitation tank and just remove the gred, and the liquid outlet of the phosphatization precipitation tank passes through tube fit the
One delivery pump connects several filters of series/parallel, positioned at the phosphating solution outlet of the filter of end or each filter
Phosphating solution outlet is connect by tube fit filter pump with phosphatization dope storage bin, the phosphatization dope storage bin by pipeline and
Second delivery pump is connect with an inverse filter, and the liquid outlet of the inverse filter passes through tube fit third delivery pump and one
Full dose filtering type slag remover connects, and the liquid outlet of full dose filtering type slag remover coordinates pipeline to connect anti-cleaning device by valve
And/or filtering film component;The liquid outlet of the anti-cleaning device is also filtered by cleaning pipe, cleaning pump and the first valve and full dose
Formula slag remover returns the connection of liquid/gas mouth, and match the anti-scavenger circuit for forming full dose filtering type slag remover;The filtering film component
Also pass through return pipe, the second valve and filter pump and the first liquid outlet of the phosphatization precipitation tank and the liquid outlet of inverse filter
Connection, the liquid outlet of the first liquid outlet, inverse filter from the phosphatization precipitation tank and full dose filtering type slag remover go out liquid
The clarification phosphating solution of mouth outflow sends the Phosphating Slot back to after filtering film component filtering by return pipe.
It is expanded on further as to above-mentioned technical proposal：
In the above-mentioned technical solutions, air-blowing mechanism is further included, if the air-blowing mechanism includes compression pump, several tracheaes and dry air
Valve, described tracheae one end are connect with the compression pump, and the other end is then precipitated with the liquid outlet of the Phosphating Slot, phosphatization respectively
The liquid/gas mouth that returns of the liquid outlet of slot, the liquid outlet of inverse filter and full dose filtering type slag remover connects;Several air valves
Door is serially connected on the matching tracheae, and several air door on/off, can make the air compressed by the compression pump
Air pipe matching is pressed into the Phosphating Slot, phosphatization precipitation tank, inverse filter and full dose filtering type slag remover, and blow off and be adhered to
Phosphating Slot, phosphatization precipitation tank, inverse filter and the phosphatization slag of full dose filtering type slag remover inner surface and/or drying phosphatization slag.
Further, the air door is pneumatic ball valve.
In the above-mentioned technical solutions, the sewage draining exit of several filters concatenates sediment pump by blow-off pipe and connects with detritus tank
It connects;Conveyance conduit and filter pump, and the delivery pipe two are set between several arbitrary two adjacent filters of filter of series connection
End connects the phosphating solution outlet of two adjacent filters respectively and inlet, the filter pump are serially connected on conveyance conduit;In parallel
Liquid outlet of the inlet of several filters with phosphatization precipitation tank docks, and phosphating solution outlet is concatenated by pipeline filters
Pump is connect with phosphatization dope storage bin.
Connect there are four in the above-mentioned technical solutions, being set between the phosphatization precipitation tank and the phosphatization dope storage bin/
Filter in parallel.
In the above-mentioned technical solutions, the filter is cyclone hydraulic separators or cartridge filter.
In the above-mentioned technical solutions, the delivery pump, the first delivery pump, the second delivery pump and third delivery pump are two-shipper
The corrosion-resistant Chinese mugwort of stainless steel is sealed than DS slagging-off circulating pumps, the filter pump is acid and alkali-resistance filter pump.
In the above-mentioned technical solutions, the valve, the first valve and the second valve are electrical ball valve, and the pipeline,
Be additionally provided with Hand-operated butterfly valve on conveyance conduit, cleaning pipe and return pipe, the Hand-operated butterfly valve for the corresponding pipeline of manual ON/OFF,
Conveyance conduit, cleaning pipe and return pipe conducting.
In the above-mentioned technical solutions, the filtering film component includes at least four MF films being sequentially connected in series or UF films, described
MF films/UF film activity pulls are installed in filter cartridge.
In the above-mentioned technical solutions, the phosphatization precipitation tank is ramp type phosphatization precipitation tank.
The beneficial effects of the invention are as follows:The application slag removing system of the present invention removes the gred by full dose filtering type slag remover
Before, by increasing cyclone hydraulic separators/cartridge filter just remove the gred, it is temporary that the dope just to remove the gred flows into phosphatization dope storage bin
It deposits, temporary phosphatization dope first removes the gred after inverse filter filters in input full dose filtering type slag remover, by multiple
Filtering, sub-sieve and slagging-off remove the phosphatization slag in phosphating solution;The slagging-off effect of the phosphorizing residue removal system of the present invention is good, can incite somebody to action
Phosphatization slag content is controlled by original more than 500ppm within 300ppm in phosphating solution, and the phosphatization for eliminating work piece surface is sunk
Slag avoids carrying out polishing processing to workpiece, improves the anti-corrosion grade of workpiece and promotes product overall quality；Meanwhile this hair
Bright phosphorizing residue removal system solves the problems, such as the easy pipeline blockage of phosphorizing residue removal system and equipment leakage, improves the profit of phosphating solution
With rate, the maintaining expense of relevant device is reduced.
Description of the drawings
In order to illustrate the technical solution of the embodiments of the present invention more clearly, it will make below to required in the embodiment of the present invention
Attached drawing is briefly described, for those of ordinary skill in the art, without creative efforts, also
Other attached drawings can be obtained according to these attached drawings.
Fig. 1 is a kind of schematic diagram of application phosphorizing residue removal system of the present invention；
Fig. 2 is another schematic diagram of application phosphorizing residue removal system of the present invention.
Specific embodiment
The invention will now be described in further detail with reference to the accompanying drawings.
The embodiment described by reference to attached drawing is exemplary, it is intended to for explaining the application, and it is not intended that right
The limitation of the application.In the description of the present application, it is to be understood that term " " center ", " longitudinal direction ", " transverse direction ", " length ",
" width ", " thickness ", " on ", " under ", "front", "rear", "left", "right", " vertical ", " level ", " top ", " bottom " " interior ", " outer ",
The orientation or position relationship of the instructions such as " clockwise ", " counterclockwise " be based on orientation shown in the drawings or position relationship, be only for
Convenient for description the application and simplify description rather than instruction or imply that signified device or element there must be specific side
Position, with specific azimuth configuration and operation, therefore it is not intended that limitation to the application.In addition, term " first ", " second "
Description purpose is only used for, and it is not intended that indicating or implying relative importance or imply the technical characteristic indicated by indicating
Quantity." first " is defined as a result, and the feature of " second " can be expressed or implicitly includes one or more spy
Sign.In the description of the present application, " several ", " multiple " are meant that two or more, unless otherwise clearly specific
It limits.In this application unless specifically defined or limited otherwise, the arts such as term " installation ", " connected ", " connection ", " fixation "
Language should be interpreted broadly, for example, it may be being fixedly connected or being detachably connected or be integrally connected;Can be machinery
Connection can also be electrical connection;It can be directly connected, can also be indirectly connected by intermediary, can be two elements
Internal connection.For the ordinary skill in the art, above-mentioned term can be understood in the application as the case may be
In concrete meaning.Unless otherwise clearly defined and limited, in this application, fisrt feature second feature it " on " or it
" under " can be in direct contact including the first and second features, it is not to be in direct contact but lead to that can also include the first and second features
Cross the other characterisation contact between them.And fisrt feature second feature " on ", " top " and " above " including
One feature is right over second feature and oblique upper, or is merely representative of fisrt feature level height higher than second feature.First is special
Sign second feature " under ", " lower section " and " below " including fisrt feature right over second feature and oblique upper, or only
Represent that fisrt feature level height is less than second feature.
Attached drawing 1-2 examples specific embodiments of the present invention, the application phosphorizing residue removal system of the application are used for large truck
His painting of driver's cabin.
Embodiment 1
Refer to the attached drawing 1, a kind of application phosphorizing residue removal system, including Phosphating Slot 1, the Phosphating Slot 1 is sunk by delivery pump 2 with phosphatization
Shallow lake slot 3 connects, and specifically concatenates liquid valve by pipeline 4 for the liquid outlet 001 of the Phosphating Slot 1（The non-label of attached drawing is often selected
Conventional Hand-operated butterfly valve）It is connect afterwards with delivery pump 2, and delivery pump 2 is connect further through pipeline 4 with phosphatization precipitation tank 3, the conveying
The phosphating solution discharged along 1 liquid outlet 001 of Phosphating Slot can be sent into the phosphatization precipitation tank 3 and just remove the gred by pump 2, in the present embodiment
In, the phosphatization precipitation tank 3 is ramp type phosphatization precipitation tank, and the liquid outlet 002 of the phosphatization precipitation tank 3 is coordinated by pipeline 4
Several filters 6 of first delivery pump 5 connection series connection, and the phosphating solution outlet 004 of the filter 6 positioned at end passes through pipeline
4 complement filters pump 7 is connect with phosphatization dope storage bin 8, and in the present embodiment, filter 6 is set as four, and filter 6
For cyclone hydraulic separators or cartridge filter, conveyance conduit 9 and filter pump 7,9 liang of the delivery pipe are set between two adjacent filters 6
End connects the phosphating solution outlet 004 of two adjacent filters 6 respectively and inlet 005, the filter pump 7 are then serially connected in conveyance conduit
On 9, filter pump 7 is since the phosphatization dope for generating filter 6 is pumped to next filter 6, and the sewage draining exit of all filters 6
006 concatenates sediment pump 11 by blow-off pipe 11 connect with detritus tank 12, and the sediment pump 11 is used to produce 6 rotary filter press of filter
Raw phosphatization slag is delivered in detritus tank 12；And the phosphatization dope that 6 rotary filter press of filter positioned at end generates can be by matching
Filter pump 7 be pumped to the phosphatization dope storage bin 8, the phosphatization dope storage bin 8 is and described for keeping in phosphatization dope
Phosphatization dope storage bin 8 is connect, and the inverse filter 14 by 4 and second delivery pump 13 of pipeline with an inverse filter 14
Liquid outlet 007 third delivery pump 15 is coordinated to be connect with a full dose filtering type slag remover 16 by pipeline 4, be temporarily stored in phosphatization dope
Phosphatization dope in storage bin 8 is pumped to the inverse filter 14 by the second delivery pump 13, and inverse filter 14 is to input
Filtering and removing slag, the phosphatization dope generated after slagging-off are pumped to full dose filtering type by third delivery pump 15 and remove the progress of phosphatization dope again
Phosphorizing residue removal, in the present embodiment, the delivery pump 2, the first delivery pump 5, the second delivery pump 13 and third are carried out in slag machine 16
Delivery pump 15, which is that two-shipper envelope stainless steel is corrosion-resistant, to end than DS slagging-off circulating pumps, and the filter pump 7 is acid and alkali-resistance filter pump;It is and complete
The liquid outlet 008 of amount filtering type slag remover 16 coordinates pipeline 4 to connect anti-cleaning device 18 and/or filtering film component by valve 17
19, in the present embodiment, the 17 preferred electrical ball valve of valve;The liquid outlet 009 of the anti-cleaning device 18 also passes through cleaning
Pipe 20,21 and first valve 22 of cleaning pump are connect, and it is complete to match composition with the liquid/gas mouth 100 that returns of full dose filtering type slag remover 16
The anti-scavenger circuit of filtering type slag remover 16 is measured, in the present embodiment, the first valve 22 is electrical ball valve;The filtering film component
19 also pass through return pipe 23, the second valve 24 and filter pump 7 and the first liquid outlet 101 of the phosphatization precipitation tank 3（This first goes out
Liquid mouth 101 is the outlet of the clear phosphatization clear liquid in upper strata）It is connected with the liquid outlet 007 of inverse filter 14, in the present embodiment,
Second valve, 24 preferred electrical ball valve, and during phosphorizing residue removal, from the first liquid outlet 101 of the phosphatization precipitation tank 3（This
One liquid outlet 101 is the outlet of the clear phosphatization clear liquid in upper strata）, inverse filter 14 liquid outlet 007 and full dose filtering type remove
The clarification phosphating solution that the liquid outlet 008 of slag machine 16 flows out is sent back to described after the filtering film component 19 filtering by return pipe 23
Phosphating Slot 1 in the present embodiment, further includes air-blowing mechanism, and the air-blowing mechanism includes compression pump 25, several tracheaes 26 and several
Air door 27, in the present embodiment, 27 preferred pneumatic ball valve of air door, and 26 one end of the tracheae with the compression pump
25 connection, the other end then respectively with the liquid outlet 001, the liquid outlet 002 of phosphatization precipitation tank 3, inverse filter of the Phosphating Slot 1
14 liquid outlet 007 and the liquid/gas mouth 100 that returns of full dose filtering type slag remover 16 connect;Several air doors 27 are serially connected in
It matches on the tracheae 26, and several air doors 27 turn on, the air pressure compressed by the compression pump 25 can be made
Tracheae matching is pressed into the Phosphating Slot 1, phosphatization precipitation tank 3, inverse filter 14 and full dose filtering type slag remover 16, and blow off viscous
Be attached to Phosphating Slot 1,16 inner surface of phosphatization precipitation tank 3, inverse filter 14 and full dose filtering type slag remover phosphatization slag and/or blow
Dry phosphatization slag；In the present embodiment, preferably, being additionally provided on the pipeline 4, conveyance conduit 9, cleaning pipe 20 and return pipe 23
Hand-operated butterfly valve（The non-label of attached drawing）, the Hand-operated butterfly valve is for the corresponding pipeline 4 of manual ON/OFF, conveyance conduit 9, cleaning pipe 20
And return pipe 23 is connected；And the filtering film component 19 includes at least four MF films being sequentially connected in series（Microfiltration membranes）Or UF films（It is super
Filter membrane）, the MF films/UF film activity pulls are installed in filter cartridge 28, and the MF films/UF film activity pulls are installed on filter cartridge
28 be for being convenient for changing matched filter membrane, so as to ensure 19 corresponding filtering function of filtering film component.
Refer to the attached drawing 1, in the present embodiment, the inverse filter 14 and phosphating solution precipitation tank 3 are all connected with matched sink
Slag bath, the phosphatization slag for being precipitated by phosphating solution precipitation tank 3 and generation being filtered by inverse filter 14 can be sent to corresponding detritus tank,
And the full dose filtering type slag remover selection patent name is：A kind of reverse filtering means dehydration one deslagging devices of full flow PS（Specially
Profit number：201420441254.2）Corresponding slagging-off frame.
It should be noted that in practice, the liquid outlet 007 of the inverse filter 14 passes through the second valve 24 and filter pump
7 connect and by pipeline 4 and third delivery pump 15 and full dose filtering type slag remover 16 with filtering film component 19, that is, in reality
During phosphorizing residue removal, it can be removed the gred according to slagging-off situation without the full dose filtering type slag remover 16, and make will be by reverse
The clarification phosphating solution that the filtering of filter 14 generates is sent back in Phosphating Slot 1, the application processing of matching Phosphating Slot 1, certainly, in order to more preferable
Slagging-off, through inverse filter 14 generate phosphatization dope remove the gred again through full dose filtering type slag remover 16, remove the gred effect
More preferably.
In the present embodiment, refer to the attached drawing 1, the anti-cleaning device 18 to full dose filtering type slag remover 16 cleaned
Cheng Wei：The valve 17 of 16 liquid outlet 008 of full dose filtering type slag remover connection filtering film component 19 is closed, and connects anti-cleaning device 18
Valve 17 open, meanwhile, first valve 22 is opened, and cleaning pump 21 is by the water in anti-cleaning device 18 along cleaning pipe 20
Pumping, and injected in full dose filtering type slag remover 16, and to full dose mistake from the liquid/gas mouth 100 that returns of full dose filtering type slag remover 16
Filter formula slag remover 16 is cleaned, and anti-cleaning device 18 can be flowed to along its liquid outlet 008 by cleaning the sewage generated, by repeatedly
Repeatedly the cleaning to full dose filtering type slag remover 16 is completed in matching.
Embodiment 2
Refer to the attached drawing 2, a kind of application phosphorizing residue removal system, including Phosphating Slot 1, the Phosphating Slot 1 is sunk by delivery pump 2 with phosphatization
Shallow lake slot 3 connects, and specifically concatenates liquid valve by pipeline 4 for the liquid outlet 001 of the Phosphating Slot 1（The non-label of attached drawing is often selected
Conventional Hand-operated butterfly valve）It is connect afterwards with delivery pump 2, and delivery pump 2 is connect further through pipeline 4 with phosphatization precipitation tank 3, the conveying
The phosphating solution discharged along 1 liquid outlet 001 of Phosphating Slot can be sent into the phosphatization precipitation tank 3 and just remove the gred by pump 2, in the present embodiment
In, the phosphatization precipitation tank 3 is ramp type phosphatization precipitation tank, and the liquid outlet 002 of the phosphatization precipitation tank 3 is coordinated by pipeline 4
First delivery pump 5 connects several filters 6 in parallel, and the inlet 005 of several filters 6 passes through pipeline 4 and phosphatization
The liquid outlet 002 of precipitation tank 3 docks, and the phosphating solution of each filter 6 outlet 004 concatenates filter pump 7 and phosphatization by pipeline 4
Dope storage bin 8 connects, and in the present embodiment, filter 6 is set as four, and filter 6 is cyclone hydraulic separators or security personnel
All filters 6 are arranged in parallel by filter, and the filtration yield of phosphating solution can be regulated and controled, and are turned on/off filtering by control
6 corresponding filter pump 7 of device, so as to control the amount of the phosphating solution in input phosphating solution storage bin 8, and the blowdown of all filters 6
Mouth 006 concatenates sediment pump 11 by blow-off pipe 11 and is connect with detritus tank 12, and the sediment pump 11 is used for 6 rotary filter press of filter
The phosphatization slag of generation is delivered in detritus tank 12；And positioned at end 6 rotary filter press of filter generate phosphatization dope can by
The filter pump 7 matched is pumped to the phosphatization dope storage bin 8, and the phosphatization dope storage bin 8 is for keeping in phosphatization dope, and institute
Phosphatization dope storage bin 8 is stated to connect, and the inverse filter with an inverse filter 14 by 4 and second delivery pump 13 of pipeline
14 liquid outlet 007 coordinates third delivery pump 15 to be connect with a full dose filtering type slag remover 16 by pipeline 4, and it is dense to be temporarily stored in phosphatization
Phosphatization dope in liquid storage bin 8 is pumped to the inverse filter 14 by the second delivery pump 13, and inverse filter 14 is to input
Phosphatization dope carry out filtering and removing slag, the phosphatization dope generated after slagging-off are pumped to full dose filtering type by third delivery pump 15 again
Phosphorizing residue removal is carried out in slag remover 16, in the present embodiment, the delivery pump 2, the first delivery pump 5, the second delivery pump 13 and the
Three delivery pumps 15, which are that two-shipper envelope stainless steel is corrosion-resistant, to end than DS slagging-off circulating pumps, and the filter pump 7 is acid and alkali-resistance filter pump;And
The liquid outlet 008 of full dose filtering type slag remover 16 coordinates pipeline 4 to connect anti-cleaning device 18 and/or filtration module by valve 17
Part 19, in the present embodiment, the 17 preferred electrical ball valve of valve;The liquid outlet 009 of the anti-cleaning device 18 is also by clear
Wash pipe 20,21 and first valve 22 of cleaning pump is connect, and match composition with the liquid/gas mouth 100 that returns of full dose filtering type slag remover 16
The anti-scavenger circuit of full dose filtering type slag remover 16, in the present embodiment, the first valve 22 are electrical ball valve;The filtration module
Part 19 also passes through return pipe 23, the second valve 24 and filter pump 7 and the first liquid outlet 101 of the phosphatization precipitation tank 3（This first
Liquid outlet 101 is the outlet of the clear phosphatization clear liquid in upper strata）It is connected with the liquid outlet 007 of inverse filter 14, in the present embodiment
In, 24 preferred electrical ball valve of the second valve, and during phosphorizing residue removal, from the first liquid outlet 101 of the phosphatization precipitation tank 3
（First liquid outlet 101 is the outlet of the clear phosphatization clear liquid in upper strata）, inverse filter 14 liquid outlet 007 and full dose filtering
The clarification phosphating solution that the liquid outlet 008 of formula slag remover 16 flows out is sent back to after the filtering film component 19 filtering by return pipe 23
The Phosphating Slot 1 in the present embodiment, further includes air-blowing mechanism, the air-blowing mechanism include compression pump 25, several tracheaes 26 and
Several air doors 27, in the present embodiment, 27 preferred pneumatic ball valve of air door, and 26 one end of the tracheae with the pressure
Contracting pump 25 connection, the other end then respectively with the liquid outlet 001 of the Phosphating Slot 1, the liquid outlet 002 of phosphatization precipitation tank 3, reverse mistake
The liquid outlet 007 of filter 14 and the liquid/gas mouth 100 that returns of full dose filtering type slag remover 16 connect;Several air doors 27 are gone here and there
It is connected on the matching tracheae 26, and several air doors 27 turn on, and can make the sky compressed by the compression pump 25
The matching of air pressure tracheae is pressed into the Phosphating Slot 1, phosphatization precipitation tank 3, inverse filter 14 and full dose filtering type slag remover 16, and blow
Fall be adhered to Phosphating Slot 1,16 inner surface of phosphatization precipitation tank 3, inverse filter 14 and full dose filtering type slag remover phosphatization slag and/
Or drying phosphatization slag；In the present embodiment, preferably, on the pipeline 4, conveyance conduit 9, cleaning pipe 20 and return pipe 23 also
Equipped with Hand-operated butterfly valve（The non-label of attached drawing）, the Hand-operated butterfly valve is for the corresponding pipeline 4 of manual ON/OFF, conveyance conduit 9, cleaning
Pipe 20 and return pipe 23 are connected；And the filtering film component 19 includes at least four MF films being sequentially connected in series（Microfiltration membranes）Or UF films
（Ultrafiltration membrane）, the MF films/UF film activity pulls are installed in filter cartridge 28, and the MF films/UF film activity pulls were installed on
It is for being convenient for changing matched filter membrane, so as to ensure 19 corresponding filtering function of filtering film component to filter box 28.
And inverse filter 14, phosphating solution precipitation tank 3, anti-cleaning device 18 are expanded on further, reference implementation example
1。
Above-described embodiment 1 and the application slag removing system of embodiment 2 carry out removing the gred it by full dose filtering type slag remover 16
Before, by increasing cyclone hydraulic separators/cartridge filter just remove the gred, the dope just to remove the gred flows into phosphatization dope storage bin 8 temporarily
It deposits, temporary phosphatization dope first removes the gred after the filtering of inverse filter 14 in input full dose filtering type slag remover 16, passes through
Multiple times of filtration, sub-sieve and slagging-off remove the phosphatization slag in phosphating solution;The slagging-off effect of the phosphorizing residue removal system of the present embodiment
It is good, phosphatization slag content in phosphating solution can be controlled by original more than 500ppm within 300ppm, eliminate work piece surface
Phosphating dregs avoid carrying out polishing processing to workpiece, improve the anti-corrosion grade of workpiece and promote product overall quality, and this
The phosphorizing residue removal system of embodiment solves the problems, such as the easy pipeline blockage of phosphorizing residue removal system and equipment leakage, improves phosphating solution
Utilization rate, reduce the maintaining expense of relevant device.
Above embodiment is merely illustrative and not limiting to the invention, therefore all according to described in present patent application range
The equivalent change or modification done of method, be included in the range of present patent application.
Claims (10)
1. a kind of application phosphorizing residue removal system, it is characterised in that, including Phosphating Slot, the Phosphating Slot is sunk by delivery pump and phosphatization
Shallow lake slot connection, and the phosphating solution discharged along Phosphating Slot liquid outlet can be sent into the phosphatization precipitation tank and just remove by the delivery pump
Slag, the liquid outlet of the phosphatization precipitation tank are connected several filters of series/parallel by the first delivery pump of tube fit, are located at
The phosphating solution outlet of the filter of end or the phosphating solution outlet of each filter pass through tube fit filter pump and phosphatization dope
Storage bin connects, and the phosphatization dope storage bin is connect by pipeline and the second delivery pump with an inverse filter, described reverse
The liquid outlet of filter is connect by tube fit third delivery pump with a full dose filtering type slag remover, full dose filtering type slag remover
Liquid outlet pass through valve pipeline coordinated to connect anti-cleaning device and/or filtering film component;The liquid outlet of the anti-cleaning device
Also it is connect, and match composition full dose with the liquid/gas mouth that returns of full dose filtering type slag remover by cleaning pipe, cleaning pump and the first valve
The anti-scavenger circuit of filtering type slag remover;The filtering film component also passes through return pipe, the second valve and filter pump and the phosphorus
The first liquid outlet for changing precipitation tank is connected with the liquid outlet of inverse filter, the first liquid outlet from the phosphatization precipitation tank, inverse
The clarification phosphating solution of the liquid outlet outflow of liquid outlet and full dose filtering type slag remover to filter is through the filtering film component mistake
The Phosphating Slot is sent back to by return pipe after filter.
2. a kind of application phosphorizing residue removal system according to claim 1, it is characterised in that, air-blowing mechanism is further included, it is described
Air-blowing mechanism includes compression pump, several tracheaes and several air doors, and described tracheae one end is connect with the compression pump, another
It is then filtered respectively with the liquid outlet of the Phosphating Slot, the liquid outlet of phosphatization precipitation tank, the liquid outlet of inverse filter and full dose at end
Formula slag remover returns the connection of liquid/gas mouth;Several air doors are serially connected on the matching tracheae, and several air valves
Door on/off can make the air air pipe compressed by the compression pump matching be pressed into the Phosphating Slot, phosphatization precipitation tank, inverse
To filter and full dose filtering type slag remover, and blow off and be adhered to Phosphating Slot, phosphatization precipitation tank, inverse filter and full dose filtering
The phosphatization slag of formula slag remover inner surface and/or drying phosphatization slag.
3. a kind of application phosphorizing residue removal system according to claim 2, which is characterized in that the air door is Pneumatic ball
Valve.
4. a kind of application phosphorizing residue removal system according to any one of claims 1 to 3, it is characterised in that, several mistakes
The sewage draining exit of filter concatenates sediment pump by blow-off pipe and is connect with detritus tank;Several arbitrary two adjacent mistakes of filter of series connection
Set conveyance conduit and filter pump between filter, and the delivery pipe both ends connect respectively two adjacent filters phosphating solution outlet and
Inlet, the filter pump are serially connected on conveyance conduit;The inlet of several filters in parallel with phosphatization precipitation tank
Liquid outlet docking, phosphating solution outlet by pipeline concatenation filter pump is connect with phosphatization dope storage bin.
5. a kind of application phosphorizing residue removal system according to claim 4, it is characterised in that, the phosphatization precipitation tank with it is described
The filter there are four series/parallel is set between phosphatization dope storage bin.
6. a kind of application phosphorizing residue removal system according to claim 5, which is characterized in that the filter is rotary filter press
Device or cartridge filter.
7. a kind of application phosphorizing residue removal system according to claim 6, it is characterised in that, the delivery pump, the first conveying
Pump, the second delivery pump and third delivery pump, which are that two-shipper envelope stainless steel is corrosion-resistant, to end than DS slagging-off circulating pumps, and the filter pump is
Acid and alkali-resistance filter pump.
8. a kind of application phosphorizing residue removal system according to claim 7, it is characterised in that, the valve, the first valve and
Second valve is electrical ball valve, and is additionally provided with Hand-operated butterfly valve on the pipeline, conveyance conduit, cleaning pipe and return pipe, described
Hand-operated butterfly valve is for the corresponding pipeline of manual ON/OFF, conveyance conduit, cleaning pipe and return pipe conducting.
9. a kind of application phosphorizing residue removal system according to claim 8, it is characterised in that, the filtering film component is included extremely
Few four MF films being sequentially connected in series or UF films, the MF films/UF film activity pulls are installed in filter cartridge.
10. a kind of application phosphorizing residue removal system according to claim 9, it is characterised in that, the phosphatization precipitation tank is oblique
Board-like phosphatization precipitation tank.
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| CN201810070990.4A CN108193203B (en) | 2018-01-25 | 2018-01-25 | A kind of coating phosphorizing residue removal system |
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| CN201810070990.4A CN108193203B (en) | 2018-01-25 | 2018-01-25 | A kind of coating phosphorizing residue removal system |
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| CN108193203A true CN108193203A (en) | 2018-06-22 |
| CN108193203B CN108193203B (en) | 2019-08-02 |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108866535A (en) * | 2018-08-30 | 2018-11-23 | 安徽江淮汽车集团股份有限公司 | A kind of phosphorizing residue removal constant flux control system |
| CN110205622A (en) * | 2019-07-10 | 2019-09-06 | 宝钢集团南通线材制品有限公司 | A kind of wire surface phosphatization Slag treatment method |
| CN110304685A (en) * | 2019-07-10 | 2019-10-08 | 宝钢集团南通线材制品有限公司 | Phosphatization slag disposal system and treatment process in a kind of wire surface process for producing line |
| CN110711763A (en) * | 2019-10-25 | 2020-01-21 | 嘉兴双军环保科技有限公司 | Phosphorization slag innocent treatment system |
| CN115287640A (en) * | 2022-07-05 | 2022-11-04 | 岚图汽车科技有限公司 | Coating descaling treatment full-line cleaning system |
Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH09141020A (en) * | 1995-11-17 | 1997-06-03 | Mitsubishi Kakoki Kaisha Ltd | Method for purifying aqueous coolant |
| JP2000325709A (en) * | 1999-05-20 | 2000-11-28 | Sodick Co Ltd | Washing apparatus for filter for electric discharge machine |
| JP2003019490A (en) * | 2001-07-09 | 2003-01-21 | Sadaaki Murakami | Treatment method for organic sewage and treatment equipment for the same |
| EP1471184A2 (en) * | 2003-04-22 | 2004-10-27 | Trasmetal S.p.A. | Mud-removal apparatus |
| CN202605820U (en) * | 2012-04-13 | 2012-12-19 | 机械工业第四设计研究院 | Phosphated slag removing device |
| CN103388141A (en) * | 2013-07-18 | 2013-11-13 | 上海宝锋工程技术有限公司 | Phosphatization liquid slag synchronous-removal system |
| CN103668145A (en) * | 2012-09-03 | 2014-03-26 | 洛阳艾笛曼机械设备有限公司 | Phosphorization and phosphorization deslagging integrated device and process |
| CN203954860U (en) * | 2014-08-07 | 2014-11-26 | 惠州市箭神环保设备有限公司 | The reverse filtering means dehydration one of a kind of full flow PS deslagging device |
| CN206052153U (en) * | 2016-09-18 | 2017-03-29 | 扬州华联涂装机械有限公司 | The online Phosphating Solution slag removing system of environment-friendly type |
| CN206334440U (en) * | 2016-12-22 | 2017-07-18 | 太仓邦达工业设备有限公司 | One kind precipitation sheet frame pressure-filtering deslagging system |
-
2018
- 2018-01-25 CN CN201810070990.4A patent/CN108193203B/en active Active
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH09141020A (en) * | 1995-11-17 | 1997-06-03 | Mitsubishi Kakoki Kaisha Ltd | Method for purifying aqueous coolant |
| JP2000325709A (en) * | 1999-05-20 | 2000-11-28 | Sodick Co Ltd | Washing apparatus for filter for electric discharge machine |
| JP2003019490A (en) * | 2001-07-09 | 2003-01-21 | Sadaaki Murakami | Treatment method for organic sewage and treatment equipment for the same |
| EP1471184A2 (en) * | 2003-04-22 | 2004-10-27 | Trasmetal S.p.A. | Mud-removal apparatus |
| CN202605820U (en) * | 2012-04-13 | 2012-12-19 | 机械工业第四设计研究院 | Phosphated slag removing device |
| CN103668145A (en) * | 2012-09-03 | 2014-03-26 | 洛阳艾笛曼机械设备有限公司 | Phosphorization and phosphorization deslagging integrated device and process |
| CN103388141A (en) * | 2013-07-18 | 2013-11-13 | 上海宝锋工程技术有限公司 | Phosphatization liquid slag synchronous-removal system |
| CN203954860U (en) * | 2014-08-07 | 2014-11-26 | 惠州市箭神环保设备有限公司 | The reverse filtering means dehydration one of a kind of full flow PS deslagging device |
| CN206052153U (en) * | 2016-09-18 | 2017-03-29 | 扬州华联涂装机械有限公司 | The online Phosphating Solution slag removing system of environment-friendly type |
| CN206334440U (en) * | 2016-12-22 | 2017-07-18 | 太仓邦达工业设备有限公司 | One kind precipitation sheet frame pressure-filtering deslagging system |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108866535A (en) * | 2018-08-30 | 2018-11-23 | 安徽江淮汽车集团股份有限公司 | A kind of phosphorizing residue removal constant flux control system |
| CN110205622A (en) * | 2019-07-10 | 2019-09-06 | 宝钢集团南通线材制品有限公司 | A kind of wire surface phosphatization Slag treatment method |
| CN110304685A (en) * | 2019-07-10 | 2019-10-08 | 宝钢集团南通线材制品有限公司 | Phosphatization slag disposal system and treatment process in a kind of wire surface process for producing line |
| CN110711763A (en) * | 2019-10-25 | 2020-01-21 | 嘉兴双军环保科技有限公司 | Phosphorization slag innocent treatment system |
| CN115287640A (en) * | 2022-07-05 | 2022-11-04 | 岚图汽车科技有限公司 | Coating descaling treatment full-line cleaning system |
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Application publication date: 20180622 Assignee: Guangdong HSBC comprehensive energy Co., Ltd Assignor: Jinan University Contract record no.: X2019440000029 Denomination of invention: Coating phosphating slag removal system Granted publication date: 20190802 License type: Common License Record date: 20191120 |