CN216173164U - Double-cavity automatic high-viscosity slurry iron remover - Google Patents
Double-cavity automatic high-viscosity slurry iron remover Download PDFInfo
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- CN216173164U CN216173164U CN202122398719.3U CN202122398719U CN216173164U CN 216173164 U CN216173164 U CN 216173164U CN 202122398719 U CN202122398719 U CN 202122398719U CN 216173164 U CN216173164 U CN 216173164U
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Abstract
The utility model discloses a double-cavity automatic high-viscosity slurry iron remover, and relates to an iron removing device, which comprises a filter cavity and a cleaning cavity, wherein a feed inlet and a discharge outlet are formed in the filter cavity, a cleaning agent inlet and a slag outlet are formed in the cleaning cavity, an openable gate valve is arranged between the filter cavity and the cleaning cavity, movable magnetic rod groups are arranged in the filter cavity and the cleaning cavity, and each magnetic rod group comprises a plurality of magnetic rods and a magnetic core which can be pulled away from the magnetic rods. Compared with the prior art, the utility model has the advantages that the deironing filtration and the slag cleaning are respectively carried out in the two cavities through the double-cavity arrangement, so that the filter cavity can run for a long time, and the problems that the cavity needs to be cleaned by long-time shutdown in the case of a single cavity, and the consumption of a cleaning agent is large and the loss of slurry is large in the case of cleaning are solved.
Description
Technical Field
The utility model relates to an iron removal device, in particular to a high-viscosity slurry iron remover.
Background
The existing slurry iron remover is a single cavity, and both the iron removing process and the cleaning process are finished in the single cavity. After the deironing goes on to the certain degree, inhale full iron fillings on the bar magnet and must clear up the bar magnet, can stop the entering of thick liquids this moment, pour into the cleaner in the cavity simultaneously and take away impurity, must be with the complete sanitization of cavity and stoving when wasing, otherwise remaining washing liquid can pollute the battery thick liquids, nevertheless if the thick liquids are that solid state content is high, the viscidity is strong, the poor thick liquids of mobility need high pressure, the high flow erodees, this makes whole cleaning process long consuming time, with high costs, the work efficiency of single de-ironing separator has seriously been influenced.
SUMMERY OF THE UTILITY MODEL
Aiming at the defects in the prior art, the utility model provides a double-cavity automatic high-viscosity slurry iron remover
In order to solve the technical problem, the utility model is solved by the following technical scheme: automatic high viscosity thick liquids de-ironing separator of double-cavity body, including filter chamber and clean chamber, the filter chamber on be provided with feed inlet and discharge gate, clean chamber on be provided with sanitizer entry and slag notch, the filter chamber with clean chamber between have an openable gate valve, filter chamber and clean intracavity are provided with mobilizable bar magnet group, the bar magnet group includes a plurality of bar magnet and can follow the magnetic core that the bar magnet was taken out from.
Preferably, in the technical scheme, a transition section is arranged between the filter cavity and the cleaning cavity, the gate valve is arranged in the transition section, the transition section is provided with a magnetic rod group limit, and the magnetic rod group limit is provided with a plurality of through holes through which the magnetic rods can pass and extend to the filter cavity.
Preferably, in the above technical scheme, a filter body is arranged in the filter cavity, the filter body is provided with a plurality of filter channels matched with the magnetic rods, the magnetic rods can move in the filter channels, and gaps are formed between the magnetic rods and the filter channels.
Preferably, in the above technical scheme, the feed inlet is located below the filter body, and the discharge outlet is located above the filter body.
Preferably, in the above technical scheme, a magnetic rod group lifting device and a magnetic core lifting device are arranged at the top of the cleaning cavity, the magnetic rod group lifting device can control the magnetic rod group to be lifted to the top in the cleaning cavity, and the magnetic core lifting device can control the magnetic core to be lifted to the outside of the cleaning cavity.
Preferably, in the technical scheme, the magnetic bar group is divided into a magnetic area and a non-magnetic area when in use, when the magnetic bar group is lifted to the top of the cleaning cavity, the cleaning agent inlet is arranged above the magnetic area, and the slag outlet is arranged below the magnetic area.
Preferably, in the above technical scheme, when the magnetic rod group abuts against the magnetic rod group limit, the magnetic rod group and the magnetic rod group limit hermetically isolate the filter cavity from the cleaning cavity.
Preferably, in the above technical scheme, the gate valve seals and isolates the filter chamber and the cleaning chamber when closed.
Preferably, in the above technical solution, a heating device is disposed in the cleaning cavity.
Preferably, in the above technical solution, the cleaning cavity is provided with an openable heat dissipation hole.
The magnetic rod can adsorb certain iron impurity after the high viscosity slurry carries out deironing, later on need clear up whole cavity, because most of need deironing's slurry all has the requirement to the purity, can not suffer from the pollution of cleaner promptly, especially lithium electricity slurry, consequently need all washd clean with the residue in the cavity in the cleaning process. For a single cavity, the iron removal process and the cleaning process are both in the same cavity, so that the whole iron removal efficiency is greatly influenced, the cavity needs to be completely cleaned during cleaning, and the residual slurry in the filter cavity is completely consumed, so that the waste is serious. The filtering and cleaning are respectively carried out in the two cavities and are not interfered with each other, and the filtering cavity can be used all the time without cleaning unless high-viscosity slurry is reloaded in the whole process. If iron impurity adsorbs when the certain degree needs to remove the dregs on the bar magnet, then only need to rise to clean chamber with bar magnet group, carry out solitary washing to the bar magnet in clean chamber, because the bar magnet structure is cylindrical basically, do not have edges and corners, directly erode can, save cleaner and cleaning time very much, simultaneously at abluent in-process, it is confined between washing chamber and the filter chamber, no matter what action takes place in the washing chamber, the filter chamber can not receive the pollution. The double cavities greatly increase the overall iron removal efficiency and reduce the loss of cleaning agents and high-viscosity slurry.
Compared with the prior art, the utility model has the advantages that the deironing filtration and the slag cleaning are respectively carried out in the two cavities through the double-cavity arrangement, so that the filter cavity can run for a long time, and the problems that the cavity needs to be cleaned by long-time shutdown in the case of a single cavity, and the consumption of a cleaning agent is large and the loss of slurry is large in the case of cleaning are solved.
Drawings
Fig. 1 is a perspective view 1 of the present invention in operation.
Fig. 2 is a perspective view 2 of the present invention in operation.
Fig. 3 is a perspective view 3 of the present invention in operation.
Fig. 4 is a perspective view 4 of the present invention in operation.
Detailed Description
Example 1: as shown in fig. 1 to 4, fig. 1 to 4 illustrate the entire filtering and cleaning process. The utility model provides an automatic high viscosity thick liquids de-ironing separator of double-cavity, includes filter chamber 1 and clean chamber 2, be provided with mobilizable bar magnet group 5 in filter chamber 1 and the clean chamber 2, bar magnet group 5 includes a plurality of bar magnet 51 and can follow the magnetic core 52 that the bar magnet was taken out and is separated. The filter cavity 1 is internally provided with a filter body 6, the filter body 6 is provided with a plurality of filter channels matched with the magnetic rods 51, the magnetic rods 51 can move in the filter channels, gaps are formed between the magnetic rods 51 and the filter channels, the width of each gap is determined by the type of slurry to be filtered, and the slurry to be filtered can only flow through the gaps between the filter channels and the magnetic rods during filtering. The filter chamber 1 on be provided with feed inlet 11 and discharge gate 12, feed inlet 11 be located filter 5 below, discharge gate 12 is located filter 5 top, this kind of flow mode from bottom to top can guarantee that all slurries can both be at the uniform velocity and even contact bar magnet 51, guarantee the adsorption effect.
The utility model discloses a filter chamber 1, including filter chamber 1, transition section 3 is provided with gate valve 4, transition section 3 on be provided with the bar magnet group spacing, the bar magnet group spacing on seted up a plurality of and can supply bar magnet 51 passes through and extends to the clearing hole of filter chamber 1. When the magnetic rod group 5 is attached to the magnetic rod group limit, the magnetic rod group 5 and the magnetic rod group limit hermetically isolate the filter cavity 1 from the cleaning cavity 2. And when the gate valve 4 is closed, the filter cavity 1 and the cleaning cavity 2 are sealed and isolated.
The top of the cleaning cavity 2 is provided with a magnetic rod group 5 lifting device, a magnetic core lifting device and a top opening, the magnetic rod group lifting device can control the magnetic rod group 5 to be lifted to the top in the cleaning cavity 1, and the magnetic core lifting device can control the magnetic core 52 to be lifted out of the cleaning cavity 1 through the top opening. The magnetic rod set 51 is divided into a magnetic area and a non-magnetic area in use, when the magnetic rod set 51 is lifted to the top in the cleaning cavity 1, the cleaning agent inlet 21 is positioned above the magnetic area, and the slag outlet 22 is positioned below the magnetic area. Cleaning chamber 2 in be provided with heating device and openable louvre, when open-top and louvre all closed, cleaning chamber 2 is encapsulated situation. The inlet 11 and outlet 12, the detergent inlet 21 and the slag outlet 22 are provided with valves.
During the use, open gate valve 4 on the changeover portion 3 for filter chamber 1 and clean chamber 2 intercommunication, then move down bar magnet group 5, let bar magnet 51 insert the filtration passageway and form the gap, bar magnet group 5 and bar magnet group limit are kneaded this moment, make and seal between filter chamber 1 and the clean chamber 2. The feed inlet 11 and the discharge outlet 12 are opened to allow the slurry to enter the filter cavity 1, the slurry slowly rises to the top of the filter cavity 1 at the bottom of the filter cavity 1, iron impurities in the slurry are adsorbed by the magnetic rod 51 when the slurry flows in the gap, and the filtered slurry flows out from the discharge outlet 12. The filter cavity 1 can be also internally provided with a monitor for monitoring the thickness of iron impurities on the magnetic rod, when the iron impurities on the magnetic rod 51 reach a certain thickness, the feed inlet 11 and the discharge outlet 12 are closed, the magnetic rod group 5 is lifted to the cleaning cavity 2, at the moment, the slurry in the filter cavity 1 can flow down to the lower part of the filter body 6, and the filtered slurry is remained above the filter body 6. The magnetic rod group 5 closes the gate valve 4 after in the clean chamber 2, lets filter chamber 1 and clean chamber 2 filter chamber sealed, then opens the open-top and continues to promote magnetic core 52 again, lets magnetic core 52 and magnetic rod 51 break away from completely for magnetic rod 51 in the clean chamber 2 becomes no magnetism district, lets iron impurity drop naturally on the magnetic rod, closes the open-top afterwards, opens sanitizer entry 21 and slag notch 22, washs clean chamber 2 through the sanitizer. After the cleaning cavity 2 is cleaned, the heating device is started to dry the cleaning cavity 2, and if the cleaning agent is nontoxic, the heat dissipation holes can be opened to dissipate heat and accelerate drying. If the cleaning agent is toxic, the heat dissipation holes are closed all the time. After cleaning chamber 2 is cleaned, magnetic core 52 is reinserted into magnetic rod 51 to form complete magnetic rod set 5, and the above steps are repeated to filter the slurry. In whole filtering step, filter chamber 1 and clean chamber 2 mutual noninterference, sealed each other, as long as do not trade thick liquids filter chamber 1 can not clear up always, and the clearance volume is little in the clean chamber 2, and the clearance is efficient, fast, and the sanitizer is expected fewly.
Claims (10)
1. Automatic high viscosity thick liquids de-ironing separator of double-chamber body, characterized in that includes filter chamber and clean chamber, the filter chamber on be provided with feed inlet and discharge gate, clean chamber on be provided with sanitizer entry and slag notch, the filter chamber with clean chamber between have an open closed gate valve, filter chamber and clean intracavity are provided with mobilizable bar magnet group, bar magnet group includes a plurality of bar magnet and can follow the magnetic core that the bar magnet was taken out away.
2. The automatic high-viscosity slurry de-ironing separator with two cavities according to claim 1, wherein a transition section is arranged between the filter cavity and the cleaning cavity, the gate valve is arranged in the transition section, the transition section is provided with a magnetic rod group limit, and the magnetic rod group limit is provided with a plurality of through holes for the magnetic rods to pass through and extend to the filter cavity.
3. The automatic high-viscosity slurry de-ironing separator with two cavities according to claim 2, wherein a filter is arranged in the filter cavity, a plurality of filter channels matched with the magnetic rods are arranged on the filter, the magnetic rods can move in the filter channels, and gaps are arranged between the magnetic rods and the filter channels.
4. The automatic high-viscosity slurry de-ironing separator with two cavities according to claim 3, wherein the feeding port is located below the filtering body, and the discharging port is located above the filtering body.
5. The dual-cavity automatic high-viscosity slurry de-ironing device according to claim 1, wherein a magnetic rod set lifting device and a magnetic core lifting device are arranged at the top of the cleaning cavity, the magnetic rod set lifting device can control the magnetic rod set to lift to the top in the cleaning cavity, and the magnetic core lifting device can control the magnetic core to lift out of the cleaning cavity.
6. The dual-cavity automatic high-viscosity slurry de-ironing separator according to claim 5, wherein the magnetic bar set is divided into a magnetic area and a non-magnetic area when in use, when the magnetic bar set is lifted to the top of the cleaning cavity, the cleaning agent inlet is above the magnetic area, and the slag outlet is below the magnetic area.
7. The dual-cavity automatic high-viscosity slurry de-ironing separator according to claim 2, wherein the filter cavity and the cleaning cavity are sealed and isolated by the magnetic rod set and the magnetic rod set limit when the magnetic rod set abuts against the magnetic rod set limit.
8. The dual-cavity automatic high-viscosity slurry de-ironing separator according to claim 1, wherein the gate valve seals the filter cavity from the cleaning cavity when closed.
9. The dual-cavity automatic high-viscosity slurry de-ironing separator as claimed in claim 1, wherein a heating device is disposed in the cleaning cavity.
10. The dual-cavity automatic high-viscosity slurry de-ironing separator according to claim 9, wherein the cleaning cavity is provided with an openable heat dissipation hole.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122398719.3U CN216173164U (en) | 2021-09-30 | 2021-09-30 | Double-cavity automatic high-viscosity slurry iron remover |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122398719.3U CN216173164U (en) | 2021-09-30 | 2021-09-30 | Double-cavity automatic high-viscosity slurry iron remover |
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| CN216173164U true CN216173164U (en) | 2022-04-05 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113976312A (en) * | 2021-09-30 | 2022-01-28 | 宁波西磁磁业发展股份有限公司 | Double-cavity automatic high-viscosity slurry iron remover |
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2021
- 2021-09-30 CN CN202122398719.3U patent/CN216173164U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113976312A (en) * | 2021-09-30 | 2022-01-28 | 宁波西磁磁业发展股份有限公司 | Double-cavity automatic high-viscosity slurry iron remover |
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Address after: 315200 No.99, Lipu Road, Shupu Town, Zhenhai District, Ningbo City, Zhejiang Province Patentee after: Ningbo West Magnetic Technology Development Co.,Ltd. Address before: 315200 No.99, Lipu Road, Shupu Town, Zhenhai District, Ningbo City, Zhejiang Province Patentee before: NINGBO SOUWEST MAGNETECH DEVELOPMENT CO.,LTD. |
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