CN205867710U - Phosphated slag removing device - Google Patents
Phosphated slag removing device Download PDFInfo
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- CN205867710U CN205867710U CN201620771504.8U CN201620771504U CN205867710U CN 205867710 U CN205867710 U CN 205867710U CN 201620771504 U CN201620771504 U CN 201620771504U CN 205867710 U CN205867710 U CN 205867710U
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- cylinder body
- water inlet
- residue
- filtering bodies
- remove device
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Abstract
The utility model discloses a phosphated slag removing device, comprising a cylinder body, the cylinder body lower extreme is connected with whirlwind formula bonderizing water inlet tube, the upper end of cylinder body is provided with the pipe of slagging tap, the cylinder body embeds there is the hollow filtering body of mistake, the upper end of crossing filtering body is provided with the working solution drain pipe of protractile cylinder body, be provided with on the whirlwind formula bonderizing water inlet tube and be used for guiding the rotatory ascending water inlet of rivers, the device is to bonderizing slagging -off process because the sediment accumulation of crossing on the filtering body attaches the phenomenon that leads to the treatment effeciency to descend, through reasonable design, especially, through at the cylinder body when intaking, cross the design that forms whirlwind formula rivers between the filtering body, realized that the long -time work of filtering body can not lead to the filter capacity to descend because the sediment accumulation attaches too much yet, do not need frequent washing, changed filtering body and can guarantee also that working solution drain pipe outflow filtrating volume remains stable, and simple structure is easy -to -use, therefore, the carrier wave prepaid electric energy meter is low in cost, be favorable to the popularization and application of technique.
Description
Technical field
This utility model relates to the technical field of metal material acid washing phosphorization, particularly a kind of Residue-remove Device In Phosphating Treatment.
Background technology
The most at home, phosphatization is conventional pretreatment technology, and steel iron phosphatising is mainly used at the bottom of anti-corrosion protection and paint
Film.During the phosphatization epithelium forming Treatment of Metal Surface, substantial amounts of phosphatization slag can be produced, suspend as removed these not in time
Tiny slag particle in medicinal liquid, then can affect the stable of tank liquor and cleaning, directly affects the qualification rate of product, it is therefore desirable to
Paint line configures slag remover.And in the phosphorous chemical industry technique of the large area Coating Pretreatment such as automobile, bus body, due to groove
Liquid is bulky, produces the quantity of slag greatly, accordingly, it would be desirable to big circulation slag removing system equipment.
The most conventional deslagging method has following 3 kinds:
1, filter press slagging-off, filter press is the capital equipment of each solid-liquid separation industry at present, its filtering surface
Long-pending big, solid-holding amount is big, is used primarily in sewage treatment industry, and by pressure filtration, ventilation is dehydrated, and it is disadvantageous in that, it is
Manual operation, manually completes deslagging shovel slag, shovels the time-consuming length of slag work, and labor intensity is big, and takes up an area face greatly, leaks serious,
Volatilization is big, and the smell is awful, easily corrodes peripheral equipment, and operation surrounding is dirtier simultaneously；
2, plane formula slag remover slagging-off, plane formula slag remover passes through pressure filtration, and ventilation dehydration realizes a blob of slag and discharges, due to
Plane slag remover filter area is little, and pump circulating load is little, and it has following deficiency, and single device cannot meet systemic circulation slagging-off need
Ask, it is impossible to accomplishing the filtration system of the big flow of large area, and dewatering time can be the longest when clinker thickness, dewatering efficiency is low, need
Want routine cleaning or change filtration core, and the filtration system of the big flow of large area that is achieved if equipped with multiple devices, then
Its input cost is high, and floor space is big；
3, PS reverse filtering and concentrating system slagging-off, this PS reverse filtering and concentrating system includes inverse filter and concentration
Groove, the medicinal liquid of slag inclusion is thrown into bottom inverse filter by circulating pump, has multiple filter bag inside inverse filter, and filter bag is pacified
Dress mode is contrary with traditional mounting means, is contained in outside metal supporting network, and the Phosphating Solution of clarification returns phosphatization through filter bag
Groove, slag is then attached to the outer surface of filter bag, and after being set the operating of time, the slag on filter bag is built up attachment and made filter
Pressure rises, and amount of filtrate starts to reduce, and now back washing Automatic Program starts.Filtrate (liquid valve and supplying valve are closed, and back washing is compressed
Air door automatically opens up, and after being set the time, the slag of filter bag surface attachment is compressed sky together with the liquid medicine of filter interior
Air-blowing falls, and discharges in thickener, and this kind of filter type is pressure filtration, underflow discharge, solves the filtration of the big flow of large area
Problem, but it cannot be dehydrated, and needs additionally to increase filter dewatering equipment and realizes, at present, the filter dewatering equipment of configuration mostly is
Import equipment, price is much more expensive.
Summary of the invention
In order to overcome the deficiencies in the prior art, this utility model provides a kind of Residue-remove Device In Phosphating Treatment.
This utility model solves its technical problem and be the technical scheme is that
A kind of Residue-remove Device In Phosphating Treatment, including cylinder body, described cylinder body lower end connects cyclone type phosphatization water water inlet pipe, described cylinder
The upper end of body is provided with residue outlet, and described cylinder body is built-in with the filtering bodies of hollow, and the upper end of described filtering bodies is provided with extended
The working solution drain pipe of cylinder body, described cyclone type phosphatization water water inlet pipe is provided with for guiding water flow rotary water inlet upwards
Mouthful.
As a preference, described filtering bodies is provided with support.
As a preference, the downside of described cylinder body and filtering bodies is inverted triangle shape.
As a preference, described filtering bodies uses filter paper to make.
As a preference, described water inlet is the nozzle of inclined design.
As a preference, described water inlet includes whirlpool and guides cover.
The beneficial effects of the utility model are: this device is led because the slag accumulation in filtering bodies is attached for phosphorizing residue removal process
Cause the phenomenon that treatment effeciency declines, by reasonably design, especially by forming rotation between cylinder body, filtering bodies when water inlet
The design of wind formula current, it is achieved filtering bodies works long hours and also filter capacity will be caused to decline because slag builds up attached too much,
Need not often to clean, change filtering bodies and also can guarantee that working solution drain pipe flows out amount of filtrate and keeps stable, and simple in construction
Easy-to-use, with low cost, the beneficially popularization and application of technology.
Accompanying drawing explanation
With embodiment, this utility model is further illustrated below in conjunction with the accompanying drawings.
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
In order to make the purpose of the application, technical scheme and advantage clearer, below in conjunction with drawings and Examples, right
This utility model is further elaborated.For the thorough explanation present invention, following description can relate to some special
Determine details.And when not having these specific detail, the present invention then may still can realize, i.e. technical staff in art uses
Herein these describe and statement others skilled in the art in art effectively introduce their work essence.This external demand
It is noted that the word " front side " used in describing below, " rear side ", " left side ", " right side ", " upside ", " downside " etc. refer to
Be the direction in accompanying drawing, word " interior " and " outward " refer respectively to the direction towards or away from particular elements geometric center, phase
Close technical staff to should not be construed as beyond the application protection domain in the adjustment that above-mentioned direction is made simply, be need not creativeness
Technology.Should be appreciated that specific embodiment described herein, only in order to explain the application, is not used to limit real protection model
Enclose.And for avoiding confusion the purpose of the present invention, due to the manufacture method known, control program, part dimension, circuit layout etc.
Technology is not it will be understood that therefore they are described in detail.With reference to Fig. 1, a kind of Residue-remove Device In Phosphating Treatment, including cylinder body 1,
Described cylinder body 1 lower end connects cyclone type phosphatization water water inlet pipe 2, and the upper end of described cylinder body 1 is provided with residue outlet 3, described cylinder body 1
Being built-in with the filtering bodies 4 of hollow, the upper end of described filtering bodies 4 is provided with the working solution drain pipe 5 of extended cylinder body 1, described rotation
It is provided with for guiding water flow rotary water inlet 6 upwards on wind formula phosphatization water water inlet pipe 2.When real work, pending
Phosphatization water enters from cyclone type phosphatization water water inlet pipe 2, and makes phosphatization water form a rotation around filtering bodies 4 by water inlet 6
Wind formula current, phosphatization water is filtered by filtering bodies 4, and the clean phosphatization working solution formed after filtration just flows from working solution drain pipe 5
Go out, and the slag charge after filtering just is discharged from residue outlet 3.These cyclone type current can play and wash away the slag being attached in filtering bodies 4
Material, thus can ensure that filtering bodies 4 to work long hours also will cause filter pressure to rise, no because slag builds up attached too much
Working solution drain pipe 5 flows out amount of filtrate and keeps stable to need often cleaning, replacing filtering bodies 4 also to can guarantee that.
Should be noted that, above-mentioned cyclone type current design, and have substantially from common cyclone separator is different.Whirlwind
Separator is to utilize centrifugal inertial force when rotating to make solid particle or impurity get rid of outside wall separately, and above-mentioned cyclone type current
Design is to be attached to the slag charge in filtering bodies 4 by current scour, and i.e. both require the most just to be not quite similar in the technology that reality is implemented,
Such as to pump, the requirement etc. of nozzle, do not enumerate.
Further embodiment, with reference to a kind of Residue-remove Device In Phosphating Treatment of Fig. 1, " embodiment " the most referred to herein refers to wrap
It is contained in special characteristic, structure or the characteristic at least one implementation of the application.Different in this manual local appearance
" in embodiment " not refers both to same embodiment, is not single or the most mutually exclusive with other embodiments reality
Execute example.Embodiment includes cylinder body 1, and described cylinder body 1 lower end connects cyclone type phosphatization water water inlet pipe 2, and the upper end of described cylinder body 1 sets
Being equipped with residue outlet 3, described cylinder body 1 is built-in with the filtering bodies 4 of hollow, and the upper end of described filtering bodies 4 is provided with extended cylinder body 1
Working solution drain pipe 5, described cyclone type phosphatization water water inlet pipe 2 is provided with for guiding water flow rotary water inlet 6 upwards, institute
The downside stating cylinder body 1 and filtering bodies 4 is inverted triangle shape, makes the phosphatization water cyclone type current that water inlet 6 injects evenly.In this reality
Executing in example, described water inlet 6 is the nozzle of inclined design, coordinates sufficiently strong hydraulic pressure by the nozzle tilted, just be enough to be formed
One cyclone type current.
Further embodiment, with reference to a kind of Residue-remove Device In Phosphating Treatment of Fig. 1, including cylinder body 1, described cylinder body 1 lower end connects to be had
Cyclone type phosphatization water water inlet pipe 2, the upper end of described cylinder body 1 is provided with residue outlet 3, and described cylinder body 1 is built-in with the filtering bodies of hollow
4, the upper end of described filtering bodies 4 is provided with the working solution drain pipe 5 of extended cylinder body 1, on described cyclone type phosphatization water water inlet pipe 2
Being provided with for guiding water flow rotary water inlet 6 upwards, described filtering bodies 4 uses filter paper to make.Arrange in described filtering bodies 4
There is support 7, be used for supporting the filtering bodies 4 that filtering bodies 4, especially filter paper are made, it is to avoid damaged because of current scour.Described enter
The mouth of a river 6 includes whirlpool and guides cover 8, guides cover 8 to make phosphatization current form a swirling water current by whirlpool.
According to above-mentioned principle, this utility model can also carry out suitable change and amendment to above-mentioned embodiment.Therefore,
This utility model is not limited to detailed description of the invention disclosed and described above, to modifications and changes more of the present utility model
Should also be as falling in scope of the claims of the present utility model.
Claims (6)
1. a Residue-remove Device In Phosphating Treatment, it is characterised in that: including cylinder body (1), described cylinder body (1) lower end connects cyclone type phosphatization
Water water inlet pipe (2), the upper end of described cylinder body (1) is provided with residue outlet (3), and described cylinder body (1) is built-in with the filtering bodies of hollow
(4), the upper end of described filtering bodies (4) is provided with the working solution drain pipe (5) of extended cylinder body (1), described cyclone type phosphatization water
It is provided with on water inlet pipe (2) for guiding water flow rotary water inlet (6) upwards.
A kind of Residue-remove Device In Phosphating Treatment the most according to claim 1, it is characterised in that: it is provided with in described filtering bodies (4) and props up
Frame (7).
A kind of Residue-remove Device In Phosphating Treatment the most according to claim 1, it is characterised in that: described cylinder body (1) and filtering bodies (4)
Downside is inverted triangle shape.
A kind of Residue-remove Device In Phosphating Treatment the most according to claim 1 and 2, it is characterised in that: described filtering bodies (4) uses filter paper
Make.
A kind of Residue-remove Device In Phosphating Treatment the most according to claim 1, it is characterised in that: described water inlet (6) is inclined design
Nozzle.
A kind of Residue-remove Device In Phosphating Treatment the most according to claim 1, it is characterised in that: described water inlet (6) includes whirlpool
Guide cover (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620771504.8U CN205867710U (en) | 2016-07-21 | 2016-07-21 | Phosphated slag removing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620771504.8U CN205867710U (en) | 2016-07-21 | 2016-07-21 | Phosphated slag removing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205867710U true CN205867710U (en) | 2017-01-11 |
Family
ID=57698450
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620771504.8U Active CN205867710U (en) | 2016-07-21 | 2016-07-21 | Phosphated slag removing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205867710U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112921315A (en) * | 2021-01-13 | 2021-06-08 | 李保艳 | Preparation process of high-strength fastener |
-
2016
- 2016-07-21 CN CN201620771504.8U patent/CN205867710U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112921315A (en) * | 2021-01-13 | 2021-06-08 | 李保艳 | Preparation process of high-strength fastener |
| CN112921315B (en) * | 2021-01-13 | 2022-12-13 | 苏州瑞弗曼智能科技有限公司 | Preparation process of high-strength fastener |
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