CN88211495U - Continuously concentrating separator - Google Patents
Continuously concentrating separator Download PDFInfo
- Publication number
- CN88211495U CN88211495U CN 88211495 CN88211495U CN88211495U CN 88211495 U CN88211495 U CN 88211495U CN 88211495 CN88211495 CN 88211495 CN 88211495 U CN88211495 U CN 88211495U CN 88211495 U CN88211495 U CN 88211495U
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- CN
- China
- Prior art keywords
- filter
- pieces
- slotted vane
- continuous concentration
- filter disc
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Abstract
The utility model relates to a continuously concentrating separator which is used to reclaim the metatitanic acid in the waste water, belonging to a filter device. The new concentrating separator of the utility model is mainly composed of a frame and a filter board. The filter board is composed of an import end piece and a tailed piece which are respectively arranged at the head end and the tailed end. The middle part is provided with a plurality of groove pieces and filter pieces, and the total number of the groove pieces and the filter pieces is odd. The groove pieces and the filter pieces are arranged in intervals. Filter cloth is arranged between the pieces to separate the groove pieces and the filter pieces. The utility model can be operated continuously and is especially suitable for the reclaiming of the metatitanic acid in the waste water in titanium dioxide industry. The utility model has the advantages of low cost and high work efficiency.
Description
A kind of continuous concentration seperator is used for the recovery of waste water metatitanic acid, belongs to filter.
At present in chemical industry, the solid particle of removing in the liquid is to adopt plate and frame filter press, solid particle moved perpendicular to filtering surface when this device filtered, the filter cake progressive additive, unload grain at last, scrub, can only interval operation move and manually unpick and wash during work, and cost is higher, operating efficiency is also carried not high.
The purpose of this utility model is to provide a kind of and can continued operation moves, and is applicable to the recovery of metatitanic acid in the titanium powder industry waste water, and can reduces cost, the concentrating and separating machine of increasing work efficiency.
The main solution of the utility model concentrating and separating machine is made up of framework, filter plate two parts.Filter plate mainly is divided into four kinds: import dististyle, slotted vane, filter disc, cauda.Framework is made of the headstock, fixed charge method end plate, after-poppet, two pull bars.Filter plate is put each a slice of head and the tail respectively by import dististyle and cauda, and slotted vane and filter disc are put in the centre, and slotted vane and filter disc then have some, add up to list, and slotted vane and filter disc put at interval, has filter cloth to be separated by between sheet and the sheet.
When the operation operation, turbid liquid is carried by pump, enter the charging hole (lower left) of import dististyle, enter slotted vane subsequently, material promptly flows from bottom to top along conduit, there is filter cloth to be separated by between slotted vane and the filter disc, solid particle is blocked continuation by filter cloth and flows forward along conduit, enter interstitial hole, the back side of ploughing under rear panel enters slotted vane, makes vortex shape from slotted vane along conduit and flows from inside to outside, enters the upper left side discharge opening at last and flows out, and the eyelet that passes liquid (clear liquid) the process filter disc of filter cloth enters top-right discharge opening, flow into clean solution tank or discharge, if upper left discharge opening (muddy liquid closes dead), then muddy liquid can flow out from middle eyelet.
Description of drawings:
Fig. 1 is the utility model concentrating and separating machine front view:
Fig. 2 is the utility model concentrating and separating trough sheet front view:
Fig. 3 is the utility model concentrating and separating trough sheet B-B cutaway view:
Fig. 4 is the utility model concentrating and separating machine filter sheet front view:
Fig. 5 is the utility model concentrating and separating machine filter sheet strong point partial view:
Fig. 6 is the utility model concentrating and separating machine filter sheet AOA cutaway view:
Following the utility model concentrating and separating machine will be further described in conjunction with the accompanying drawings:
As shown in Figure 1, 2, continuous concentration seperator framework is made up of the headstock 13, fixed charge method end plate 12, after-poppet 10 and two pull bars 11, then filter plate is seated on the framework.The formation of filter plate: promptly be that filter cloth, filter disc, filter cloth, slotted vane are arranged down in proper order again after the plastics washer 1, rubber washer 2, import dististyle 3, filter cloth 4, filter disc 5, filter cloth 4 ' slotted vane 7, slotted vane is 13 altogether, filter disc is 14, put cauda 6 at last, rubber washer 16, movable dististyle 8, after all discharge, be used for movable dististyle that very heavy or electric plating propulsion 9 promotes to have pulley 14 and will put in order the group slice, thin piece and compress.Plastic pallet 15 holds the liquid that leaks down, slotted vane shown in Fig. 2,3, the slotted vane positive and negative respectively have maintain a certain distance between five conduits, the conduit and certain groove weir wide, the slotted vane centre bore is right-hand to have an eyelet and it to communicate.Slotted vane obverse and reverse structure is identical, but flows to opposite.
The structure of filter disc and slotted vane is basic identical, shown in Fig. 4,5,6, the filter disc positive and negative equally also respectively has five conduits, and the strong point of marshalling is arranged between groove weir and the groove weir, and strong point material is made for the rubber material, four rows are arranged between every conduit, and there is certain distance the centre, and short relatively near groove weir two back gauges, each fulcrum also has certain height, the upper right side of every filter disc all is equipped with eyelet, leads to the clear liquid apopore.
The utility model compared with prior art has the following advantages: the continuous concentration seperator can continued operation, availablely manually unpick and wash, and the recovery of the metatitanic acid in the particularly suitable titanium powder industry waste water, and can reduce cost, increase work efficiency.
Claims (7)
1, a kind of continuous concentration seperator is used for the recovery of waste water metatitanic acid, belong to filter, it is characterized in that it is made up of framework, filter plate two parts, framework is made of the headstock, fixed charge method end plate, after-poppet, two pull bars, and filter plate is put each a slice of head and the tail respectively by import dististyle, cauda, and slotted vane and filter disc are put in the centre, slotted vane and filter disc have some, add up to list, slotted vane and filter disc are put at interval, have filter cloth to be separated by between sheet and the sheet.
2, continuous concentration seperator according to claim 1 is characterized in that described slotted vane positive and negative respectively has five conduits.
3, continuous concentration seperator according to claim 1 is characterized in that described filter disc positive and negative respectively has five conduits.
4, continuous concentration seperator according to claim 2 is characterized in that right-handly on the described slotted vane having an eyelet and slotted vane centre bore to communicate.
5, continuous concentration seperator according to claim 3 is characterized in that having between the described filter disc groove weir strong point of marshalling.
6, continuous concentration seperator according to claim 5 is characterized in that the described strong point adopts the rubber material to make.
7, continuous concentration seperator according to claim 1 is characterized in that described filter disc upper right side is equipped with eyelet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 88211495 CN88211495U (en) | 1988-03-05 | 1988-03-05 | Continuously concentrating separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 88211495 CN88211495U (en) | 1988-03-05 | 1988-03-05 | Continuously concentrating separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN88211495U true CN88211495U (en) | 1988-12-28 |
Family
ID=4844892
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 88211495 Withdrawn CN88211495U (en) | 1988-03-05 | 1988-03-05 | Continuously concentrating separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN88211495U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101913719A (en) * | 2010-08-17 | 2010-12-15 | 安徽金星钛白（集团）有限公司 | Recovery system and recovery method of materials in titanium white wastewater |
| CN102276086A (en) * | 2011-07-21 | 2011-12-14 | 同济大学 | Centrifugation-microflocculation combined method for regeneration treatment of titanium dioxide production wastewater |
| CN103861342A (en) * | 2012-12-12 | 2014-06-18 | 江苏森美铝颜料有限公司 | High temperature refined oil purifying system |
-
1988
- 1988-03-05 CN CN 88211495 patent/CN88211495U/en not_active Withdrawn
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101913719A (en) * | 2010-08-17 | 2010-12-15 | 安徽金星钛白（集团）有限公司 | Recovery system and recovery method of materials in titanium white wastewater |
| CN101913719B (en) * | 2010-08-17 | 2012-08-22 | 安徽金星钛白（集团）有限公司 | Recovery system and recovery method of materials in titanium white wastewater |
| CN102276086A (en) * | 2011-07-21 | 2011-12-14 | 同济大学 | Centrifugation-microflocculation combined method for regeneration treatment of titanium dioxide production wastewater |
| CN103861342A (en) * | 2012-12-12 | 2014-06-18 | 江苏森美铝颜料有限公司 | High temperature refined oil purifying system |
| CN103861342B (en) * | 2012-12-12 | 2015-11-18 | 江苏森美铝颜料有限公司 | Oil-cleaning system after a kind of high temperature refines |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |