CN202605820U - Phosphated slag removing device - Google Patents
Phosphated slag removing device Download PDFInfo
- Publication number
- CN202605820U CN202605820U CN2012201555600U CN201220155560U CN202605820U CN 202605820 U CN202605820 U CN 202605820U CN 2012201555600 U CN2012201555600 U CN 2012201555600U CN 201220155560 U CN201220155560 U CN 201220155560U CN 202605820 U CN202605820 U CN 202605820U
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- CN
- China
- Prior art keywords
- phosphatization
- filter press
- frame filter
- automatic plate
- slag removing
- 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.)
- Expired - Fee Related
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Abstract
The utility model discloses a phosphated slag removing device, and relates to a slag removing device for removing phosphated slag remained in a phosphatization tank after production in the phosphatization tank. The phosphated slag removing device mainly comprises an automatic plate-and-frame filter press, a pneumatic control device, a phosphated slag removing water pump, a hydraulic control cabinet, an electronic control system and a phosphatization tank. A water inlet pipe of the automatic plate-and-frame filter press is connected with a drain outlet at the bottom of the phosphatization tank by the phosphated slag removing water pump and a pipeline, a drain pipe of the automatic plate-and-frame filter press is connected with a water inlet of the phosphatization tank by a pipeline, the pneumatic control device is further arranged on one side of the automatic plate-and-frame filter press and comprises a material inlet pneumatic valve and a compressed air reverse blowing port pneumatic valve, and the material inlet pneumatic valve and the compressed air reverse blowing port pneumatic valve are connected with the automatic plate-and-frame filter press. The phosphated slag removing device is simple in structure and reasonable in arrangement, phosphated slag remained in the phosphatization tank after production in the tank can be effectively removed, space for slag removing equipment is saved, drainage of waste liquid is reduced, and purposes of saving energy and protecting environments are achieved.
Description
Technical field
The utility model relates to a kind of interior deslagging device of leaving over the phosphatization slag, a kind of specifically phosphatization deslagging device produced of phosphatization groove groove that be used to get rid of.
Background technology
At present, conventional phosphatization deslagging device is made up of a plurality of slag removal equipments, and it is big that it occupies spatial area; The discharging of waste liquid amount is also big, in use remains in deficiency, because its complex structure; Be provided with unreasonablely, can not effectively get rid of and produce the phosphatization slag of leaving in the phosphatization groove groove, cause the waste of the energy; Can not reach the purpose of energy-conserving and environment-protective, thereby strengthen financial burden to enterprise.
The utility model content
The purpose of the utility model is to be the deficiency that solves the problems of the technologies described above, and a kind of phosphatization deslagging device is provided, and is simple in structure, be provided with rationally; Can effectively get rid of to produce in the phosphatization groove groove and leave over the phosphatization slag; Practice thrift the slag removal equipment space, reduce discharging of waste liquid, reach the purpose of energy-conserving and environment-protective.
The utility model is that to solve the problems of the technologies described above the technical scheme that is adopted be a kind of phosphatization deslagging device; Mainly form by automatic plate and frame filter press, air control unit, phosphatization slagging-off water pump, hydraulic control cabinet, electric-control system and phosphatization groove; Automatically the water inlet pipe of plate and frame filter press is connected through the discharge outlet of phosphatization slagging-off water pump and pipeline phosphatization trench bottom; Automatically the drainpipe of plate and frame filter press is connected with the water inlet of phosphatization groove through pipeline; Side at automatic plate and frame filter press also is provided with air control unit; Described air control unit comprises a charging aperture pneumatic operated valve and a compressed air back blow port pneumatic operated valve, and the charging aperture pneumatic operated valve of air control unit is connected with automatic plate and frame filter press with compressed air back blow port pneumatic operated valve.
The utility model, the water inlet pipe of described automatic plate and frame filter press are provided with the nitric acid outlet, and drainpipe is provided with the nitric acid inlet.
The beneficial effect of the utility model is: it is simple in structure, be provided with rationally; Automatically plate and frame filter press is the full-automatic plate-frame filtering system of PLC control; Be used for removing the removal of the phosphatization liquid phosphatization slag of pre-treatment, electric-control system with to supply with phosphatization slagging-off water pump control system linked, is realized the automatic completion of the work such as liquid supply, filtration, the removal of unnecessary filtrating, filter frame switching of system through flow signal; Practice thrift the slag removal equipment space; Reduce discharging of waste liquid, effectively get rid of to produce in the phosphatization groove groove and leave over the phosphatization slag, reached the purpose of energy-conserving and environment-protective.
Description of drawings
Fig. 1 is the structural representation of the utility model;
Mark among the figure: 1, automatic plate and frame filter press, 2, air control unit, 3, phosphatization slagging-off water pump, 4, the hydraulic control cabinet; 5, electric-control system, 6, the phosphatization groove, 7, water inlet pipe, 8, drainpipe; 9, discharge outlet, 10, water inlet, 11, the nitric acid outlet, 12, the nitric acid inlet.
The specific embodiment
As shown in the figure, a kind of phosphatization deslagging device mainly is made up of automatic plate and frame filter press 1, air control unit 2, phosphatization slagging-off water pump 3, hydraulic control cabinet 4, electric-control system 5 and phosphatization groove 6; Automatically the water inlet pipe 7 of plate and frame filter press 1 is connected through the discharge outlet 9 of phosphatization slagging-off water pump 3 and pipeline phosphatization groove 6 bottoms, and the drainpipe 8 of plate and frame filter press 1 passes through pipeline and is connected with the water inlet 10 of phosphatization groove 6 automatically, also is provided with air control unit 2 in a side of automatic plate and frame filter press 1; Described air control unit 2 comprises a charging aperture pneumatic operated valve and a compressed air back blow port pneumatic operated valve, and the charging aperture pneumatic operated valve of air control unit 2 is connected with automatic plate and frame filter press 1 with compressed air back blow port pneumatic operated valve, and the water inlet pipe 7 of described automatic plate and frame filter press 1 is provided with nitric acid outlet 11; Drainpipe 8 is provided with nitric acid inlet 12; Be ready to automatic plate and frame filter press 1 state, pressurize, the phosphatization slag remover starts; Squeeze into phosphatization liquid in the phosphatization slag remover through phosphatization slagging-off water pump 3; Compressed air blowback phosphatization slag remover blows the phosphatization liquid of the inside in the rephosphorization groove 6, and clean phosphatization liquid returns in the phosphatization groove 6; Filter out the filter residue that contains in the phosphatization liquid through automatic plate and frame filter press 1 then; Turnover panel is opened below pressurize end, the phosphatization slag remover, and filter cake backhaul, mobile sheet frame are opened successively, and filter residue is got rid of in discharging.
Systemic-function of described the utility model and equipment and technology parameter
:
One, systemic-function
1, through hydraulic means each filter plate is compressed;
2, control system makes and supplies with phosphatization slagging-off water pump to system's conveying phosphatization liquid through signal output;
3, control system makes supply phosphatization slagging-off water pump stop to carry phosphatization liquid to system through signal output;
4, compressed air gets into system, and filter cake is carried out second dehydration;
5, through hydraulic means, one by one each filter disc is unloaded cake, compresses;
6, phosphatization liquid import and export main line all is furnished with the nitric acid import and export, regularly cleans filter cake through nitric acid.
Two, technical parameter
1, produces the quantity of slag: 4 kg/h;
2, phosphatization tank liquor slag inclusion requires: < 200ppm;
3, phosphatization slag liquid feed liquor amount: 20m
2/ h;
4, phosphatization slag water content requirement: < 57%;
5, sheet frame: 800 * 800 * 65 (mm);
6, normal capacity: (480L);
7, filter cake thickness: 30mm;
8, filter area: 30 m
2
9, filter chamber quantity: 30 (1 on top board, 29 of middle plates, 1 of tailgate);
10, filter plate weight: about 28kg/;
11, complete machine gross weight: about 3050kg;
12, complete machine general power: 4.5kW;
13, automatic plate and frame filter press partial parameters;
14, there is the material of overcurrent part to be the SUS316 stainless steel;
15, phosphatization liquid circulation import: one, DN65, SUS316 steel flange;
16, phosphatization liquid loop exit: one, DN65, SUS316 steel flange;
17, compressed air mouth: one, DN32 galvanized pipe flange-interface;
18, acid solution and rinse water inlet: one, DN50, SUS316 steel flange;
19, acid solution and rinse water outlet: one, DN50, SUS316 steel flange;
20, connect the liquid bath floss hole: one, DN65, SUS316 steel flange;
21, Compressed Gas: the 85m that is interrupted
3/ h, operating pressure: 6bar;
22, hydraulic pressure: operating pressure 18MPa/ maximum pressure 31.5MPa.
The utility model, it is simple in structure, be provided with rationally, can effectively get rid of to produce in the phosphatization groove groove and leave over the phosphatization slag; Practice thrift the slag removal equipment space; Reduce discharging of waste liquid, the purpose that has reached energy-conserving and environment-protective has been saved the expense of enterprise, thereby has reduced the financial burden of enterprise.
Claims (2)
1. phosphatization deslagging device; Mainly form by automatic plate and frame filter press (1), air control unit (2), phosphatization slagging-off water pump (3), hydraulic control cabinet (4), electric-control system (5) and phosphatization groove (6); It is characterized in that: the water inlet pipe (7) of plate and frame filter press (1) is connected through the discharge outlet (9) of phosphatization slagging-off water pump (3) with pipeline phosphatization groove (6) bottom automatically; Automatically the drainpipe (8) of plate and frame filter press (1) is connected with the water inlet (10) of phosphatization groove (6) through pipeline; Side at automatic plate and frame filter press (1) also is provided with air control unit (2); Described air control unit (2) comprises a charging aperture pneumatic operated valve and a compressed air back blow port pneumatic operated valve, and the charging aperture pneumatic operated valve of air control unit (2) is connected with automatic plate and frame filter press (1) with compressed air back blow port pneumatic operated valve.
2. a kind of phosphatization deslagging device as claimed in claim 1 is characterized in that: the water inlet pipe (7) of described automatic plate and frame filter press (1) is provided with nitric acid outlet (11), and drainpipe (8) is provided with nitric acid inlet (12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012201555600U CN202605820U (en) | 2012-04-13 | 2012-04-13 | Phosphated slag removing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012201555600U CN202605820U (en) | 2012-04-13 | 2012-04-13 | Phosphated slag removing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202605820U true CN202605820U (en) | 2012-12-19 |
Family
ID=47339554
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012201555600U Expired - Fee Related CN202605820U (en) | 2012-04-13 | 2012-04-13 | Phosphated slag removing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202605820U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108193203A (en) * | 2018-01-25 | 2018-06-22 | 暨南大学 | A kind of application phosphorizing residue removal system |
| 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 |
| CN108998788A (en) * | 2018-08-30 | 2018-12-14 | 安徽江淮汽车集团股份有限公司 | A kind of Isobarically Control slag removing system |
| CN109647021A (en) * | 2019-02-25 | 2019-04-19 | 浙江杰为凯环保科技有限公司 | By the working method of the phosphating solution slagging-off filter press of PLC control |
| CN112426759A (en) * | 2020-11-30 | 2021-03-02 | 中国航发动力股份有限公司 | Automatic electrolyte filter press and working method thereof |
-
2012
- 2012-04-13 CN CN2012201555600U patent/CN202605820U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108193203A (en) * | 2018-01-25 | 2018-06-22 | 暨南大学 | A kind of application phosphorizing residue removal system |
| 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 |
| CN108998788A (en) * | 2018-08-30 | 2018-12-14 | 安徽江淮汽车集团股份有限公司 | A kind of Isobarically Control slag removing system |
| CN109647021A (en) * | 2019-02-25 | 2019-04-19 | 浙江杰为凯环保科技有限公司 | By the working method of the phosphating solution slagging-off filter press of PLC control |
| CN112426759A (en) * | 2020-11-30 | 2021-03-02 | 中国航发动力股份有限公司 | Automatic electrolyte filter press and working method thereof |
| CN112426759B (en) * | 2020-11-30 | 2023-04-07 | 中国航发动力股份有限公司 | Automatic electrolyte filter press and working method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: MECHANICAL INDUSTRY FOURTH DESIGN + RESEARCH INSTI Free format text: FORMER NAME: NO.4 MACHINERY INDUSTRY DESIGN INST. |
|
| CP01 | Change in the name or title of a patent holder |
Address after: 471000 Xiyuan Road, Jianxi District, Henan, No. 13, No. Patentee after: Mechanical Industry fourth Design & Research Institute Co., Ltd. Address before: 471000 Xiyuan Road, Jianxi District, Henan, No. 13, No. Patentee before: No.4 Machinery Industry Design Inst. |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121219 Termination date: 20190413 |