CN2843580Y - Filtration, washing, drying process integrated apparatus - Google Patents
Filtration, washing, drying process integrated apparatus Download PDFInfo
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- CN2843580Y CN2843580Y CN 200520120482 CN200520120482U CN2843580Y CN 2843580 Y CN2843580 Y CN 2843580Y CN 200520120482 CN200520120482 CN 200520120482 CN 200520120482 U CN200520120482 U CN 200520120482U CN 2843580 Y CN2843580 Y CN 2843580Y
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- drying process
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Abstract
The utility model relates to a kind of filtration, washing, drying process integrated apparatus, it has a container, be provided with inlet, leakage fluid dram, air inlet, exhaust outlet and slag-drip opening in this container, cleaning solution used in the washing operation injects container by described inlet, also be provided with nozzle on the described container, described nozzle is connected with an air supply system.The utility model is integrated in one filtration, washing, drying process, it is when washing operation, avoid adopting and utilize the churned mechanically mode of paddle in the aforementioned prior art, but make cleaning solution form turbulent flow by the air-flow of nozzle ejection, the solids that forms filter cake is stirred, thereby solid-liquid is fully mixed, reach good clean result, its simple in structure, easy to operate, good effect of separating solid from liquid.
Description
[technical field]
The utility model relates to a kind of solidliquid mixture separator, relates in particular to a kind of solidliquid mixture separator that integrates filtration, washing, drying process.
[background technology]
In the modern industry production process, many products all need intermediate product just can be obtained through technological operations such as filtration, washing, dryings, in order to obtain function admirable, stay-in-grade product, the said units operational group must be synthesized technological process operation pipeline smoothly.This streamline relates to a large amount of unit operating equipments and material transfer device, take not only that production site is big, equipment investment/mounting cost height, operating personnel disperse, labour intensity is big, the logistics link is big, shortcomings such as impurity are easily introduced in operating process, has restricted the production of product but also exist.
In order to address the above problem, industry attempts unit operations such as filtration, washing, drying are combined, and finishes on a set of equipment.At present, a kind of equipment wherein has container, is provided with elements such as inlet, leakage fluid dram, air inlet, exhaust outlet, paddle, slag-drip opening in this container.When the said equipment carries out the solidliquid mixture separation, at first, carry out filter operation: after solidliquid mixture is added said vesse, with inlet, the valve closing of exhaust outlet and slag-drip opening, air inlet is connected with air supply system, and leakage fluid dram is connected with drainage system, opens the valve of air inlet and leakage fluid dram, start air supply system, injecting gas in container reaches required value until pressure, closes air inlet, when pressure drops to a certain numerical value, open the valve of air inlet once more, injecting gas in container, repeatable operation, all be discharged from container until liquid, promptly finish filter operation; Then, carry out washing operation: close the valve of leakage fluid dram, the disconnection air supply system is connected with air inlet, in container, inject an amount of washing liquid, close air inlet then, paddle is linked to each other with motor, cleaning solution is under the stirring action of paddle, the solids that forms filter cake is stirred, solid-liquid is mixed, reach clean result, repeat above-mentioned filter operation, liquid in the container is discharged, promptly finish washing operation; Afterwards, carry out drying process: air inlet is connected with air supply system, starts air supply system, in container, inject the gas of uniform temperature, keep a period of time after, with the filter cake oven dry, promptly finish drying operation; At last, whole operations are promptly finished in dried material taking-up.
What above-mentioned separator adopted in filter operation is the mode of press filtration, for making the certain pressure of maintenance in the container, its sealing property to container is had relatively high expectations, yet, above-mentioned separator is to adopt churned mechanically mode when washing operation, the sealing of container is difficult to be done, and this certainly will cause guarantees that the required cost of seal of vessel performance is higher.On the other hand, the complex structure of above-mentioned mechanical agitation mode, complicated operation, deslagging difficulty, and, because there are certain clearance in the bottom of paddle and the bottom of container, therefore, paddle can not make the solid-liquid of container bottom fully mix, have residue in the container, the effect of its separation is relatively poor.
[utility model content]
Technical problem to be solved in the utility model is to provide a kind of filtration, washing, drying process integrated apparatus, its simple in structure, easy to operate, good effect of separating solid from liquid.
For solving the problems of the technologies described above, the technical scheme that the utility model adopted is: a kind of filtration, washing, drying process integrated apparatus are provided, it has a container, be provided with inlet, leakage fluid dram, air inlet, exhaust outlet and slag-drip opening in this container, cleaning solution used in the washing operation injects container by described inlet, also be provided with nozzle on the described container, described nozzle is connected with an air supply system.
As further improvement in the technical proposal, described separator also comprises the turner that is used to make described container upset, and described turner is installed on the support.
As further improvement in the technical proposal, described container is provided with inflatable mouth, and described inflatable mouth is connected with described air supply system, and it is positioned on the relative direction of described slag-drip opening.
As further improvement in the technical proposal, gas used in the drying process injects container by described air inlet or nozzle.
As further improvement in the technical proposal, described air inlet is connected with described air supply system, and described air supply system can provide the gas of different temperatures.
As further improvement in the technical proposal, described air inlet is positioned at the position of leaning on the top on the described container.
As further improvement in the technical proposal, described nozzle is positioned at the position of leaning on the below on the described container.
As further improvement in the technical proposal, near leakage fluid dram, be provided with filter medium on the described container.
As further improvement in the technical proposal, described filter medium is at least a in filter paper, filter cloth, the sintering net.
The utility model is integrated in one filtration, washing, drying process, it is when washing operation, avoid adopting and utilize the churned mechanically mode of paddle in the aforementioned prior art, but make cleaning solution form turbulent flow by the air-flow of nozzle ejection, the solids that forms filter cake is stirred, thereby solid-liquid is fully mixed, reach good clean result, its simple in structure, easy to operate, good effect of separating solid from liquid.
[description of drawings]
The utility model is described in further detail below in conjunction with the drawings and specific embodiments:
Fig. 1 is the schematic diagram of the utility model one preferred embodiment.
[specific embodiment]
See also Fig. 1, it is a preferred embodiment of the present utility model, it has a container 10, the upper end of this container 10 has the conical surface, is provided with assemblies such as inlet 11, leakage fluid dram 12, air inlet 13, exhaust outlet 14, slag-drip opening 15, nozzle 16, inflatable mouth 17, filter medium 18, turner 19 in container 10.This air inlet 11, nozzle 16 and inflatable mouth 17 are connected with an air supply system 20, and this air supply system 20 can provide the gas of different temperatures.Inlet 11, air inlet 13 and exhaust outlet 14 are positioned on the conical surface of container 10.Slag-drip opening 15 is positioned at the top of container 10, and nozzle 16 is positioned at the position of leaning on the below on the container 10, and inflatable mouth 17 is positioned on the relative direction of slag-drip opening 15, promptly is positioned at the bottom of container 10, so that the material of drying is blown out container 10.Leakage fluid dram 12 is positioned at the bottom of container 10, and filter medium 18 is positioned near the position of leakage fluid dram 12 tops, and it can be at least a in filter paper, filter cloth, the sintering net.Turner 19 is installed on the support 30, and it can make container 10 upsets.
Solidliquid mixture with the separation of hydrogen nickel oxide is an example below, and the course of work of integrated apparatus provided by the utility model is elaborated.
Behind 750 liters of adding containers 10 of solidliquid mixture of nickel hydroxide with the reaction gained, carry out filter operation.Valve closing with inlet 11, exhaust outlet 14 and slag-drip opening 15 and nozzle 16, air inlet 13 is connected with air supply system 20, leakage fluid dram 12 is connected with the drainage system (not shown), open the valve of air inlet 13 and leakage fluid dram 12, start air supply system 20, injecting gas in container 10, reach 0.35MPa until pressure, close air inlet 13, when pressure drops to 0.3MPa, open the valve of air inlet 13 once more, injecting gas in container 10, repeatable operation all is discharged from container 10 until liquid, promptly finishes filter operation.The mode of press filtration is adopted in above-mentioned filter operation, for different solidliquid mixtures, the pressure in the container 10 can be 0.1～1.0MPa, certainly, also can adopt the mode of suction filtration, the vacuum between filter medium 18 and the leakage fluid dram 12 can be-0.01～-0.2MPa.
Then, carry out washing operation.Close the valve of leakage fluid dram 12, disconnection air supply system 20 is connected with air inlet 13, in container 10, inject 600 premium on currency, close air inlet 13 then, nozzle 16 is connected with air supply system 20, open the valve of nozzle 16, close the valve of inlet 11, start air supply system 20, water forms turbulent flow under the effect of the air-flow that nozzle 16 sprays, the solids that forms filter cake is stirred, solidliquid mixture is fully mixed, stir after 30 minutes, stop to stir, repeat above-mentioned filter operation, the water in the container 10 is discharged, promptly finish washing operation.
Afterwards, carry out drying process: air inlet 13 is connected with air supply system 20, starts air supply system 20, to container 10 in, inject 100 ℃ gas, keep 1 hour after, filter cake is dried, promptly finish drying operation.In the above-mentioned drying process, also nozzle 16 can be connected with air supply system 20, by nozzle 16 injecting gas in container 10.
At last, closeall valve, the opening operation device is connected with all of the external world, start turner 19, with the conical surface of container 10 down, inflatable mouth 17 is connected with air supply system 20, connect product gathering-device (not shown) for 15 times at slag-drip opening, open slag-drip opening 15, inflatable mouth 17,, promptly finish whole operations the dried nickel hydroxide gathering-device of packing into.
After testing, the weight percent content that adopts the water of the isolated nickel hydroxide of above-mentioned separator is 1%, and the weight percent content of sulfate radical is 0.4%, reach nickel hydroxide technical requirement.
The quantity of above-mentioned inlet 11, leakage fluid dram 12, air inlet 13, exhaust outlet 14, slag-drip opening 15, inflatable mouth 17 and form can be done suitable adjustment according to actual needs; The quantity of said nozzle 16 and the relation of arranging on container 10 also can adjust according to actual needs.
Integrated apparatus of the present utility model is integrated in one filtration, washing, drying process, it is when washing operation, avoid adopting and utilize the churned mechanically mode of paddle in the aforementioned prior art, but make cleaning solution form turbulent flow by the air-flow that nozzle 16 sprays, the solids that forms filter cake is stirred, thereby solid-liquid is fully mixed, reach good clean result, its simple in structure, easy to operate, good effect of separating solid from liquid.
Claims (9)
1, a kind of filtration, washing, drying process integrated apparatus, has a container, be provided with inlet, leakage fluid dram, air inlet, exhaust outlet and slag-drip opening in this container, cleaning solution used in the washing operation injects container by described inlet, it is characterized in that: also be provided with nozzle on the described container, described nozzle is connected with an air supply system.
2, filtration as claimed in claim 1, washing, drying process integrated apparatus is characterized in that: described separator also comprises the turner that is used to make described container upset, and described turner is installed on the support.
3, filtration as claimed in claim 1, washing, drying process integrated apparatus is characterized in that: described container is provided with inflatable mouth, and described inflatable mouth is connected with described air supply system, and it is positioned on the relative direction of described slag-drip opening.
4, filtration as claimed in claim 1, washing, drying process integrated apparatus is characterized in that: gas used in the drying process injects container by described air inlet or nozzle.
5, filtration as claimed in claim 4, washing, drying process integrated apparatus is characterized in that: described air inlet is connected with described air supply system, and described air supply system can provide the gas of different temperatures.
6, filtration as claimed in claim 1, washing, drying process integrated apparatus is characterized in that: described air inlet is positioned at the position of leaning on the top on the described container.
7, filtration as claimed in claim 1, washing, drying process integrated apparatus is characterized in that: described nozzle is positioned at the position of leaning on the below on the described container.
8, as any described filtration, washing, drying process integrated apparatus in the claim 1 to 7, it is characterized in that: near leakage fluid dram, be provided with filter medium on the described container.
9, filtration as claimed in claim 8, washing, drying process integrated apparatus is characterized in that: described filter medium is at least a in filter paper, filter cloth, the sintering net.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520120482 CN2843580Y (en) | 2005-12-10 | 2005-12-10 | Filtration, washing, drying process integrated apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520120482 CN2843580Y (en) | 2005-12-10 | 2005-12-10 | Filtration, washing, drying process integrated apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2843580Y true CN2843580Y (en) | 2006-12-06 |
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ID=37485536
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200520120482 Expired - Lifetime CN2843580Y (en) | 2005-12-10 | 2005-12-10 | Filtration, washing, drying process integrated apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2843580Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103213778A (en) * | 2013-04-26 | 2013-07-24 | 张家港韩中深冷科技有限公司 | Strain strengthening storage tank |
| CN102159810B (en) * | 2008-09-19 | 2013-11-13 | 雷诺卡车公司 | Mixing device in exhaust gas pipe |
| CN108241050A (en) * | 2017-12-30 | 2018-07-03 | 西安科技大学 | A kind of reciprocating Leaching Experiments device and experimental method |
-
2005
- 2005-12-10 CN CN 200520120482 patent/CN2843580Y/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102159810B (en) * | 2008-09-19 | 2013-11-13 | 雷诺卡车公司 | Mixing device in exhaust gas pipe |
| US8745978B2 (en) | 2008-09-19 | 2014-06-10 | Renault Trucks | Mixing device in an exhaust gas pipe |
| US9097161B2 (en) | 2008-09-19 | 2015-08-04 | Volvo Trucks AB | Mixing device in an exhaust gas pipe |
| CN103213778A (en) * | 2013-04-26 | 2013-07-24 | 张家港韩中深冷科技有限公司 | Strain strengthening storage tank |
| CN108241050A (en) * | 2017-12-30 | 2018-07-03 | 西安科技大学 | A kind of reciprocating Leaching Experiments device and experimental method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20061206 |
|
| EXPY | Termination of patent right or utility model |