CN212039868U - Micro-differential pressure thickening or filtering equipment and multistage combined thickening or filtering device - Google Patents
Micro-differential pressure thickening or filtering equipment and multistage combined thickening or filtering device Download PDFInfo
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- CN212039868U CN212039868U CN202020295993.0U CN202020295993U CN212039868U CN 212039868 U CN212039868 U CN 212039868U CN 202020295993 U CN202020295993 U CN 202020295993U CN 212039868 U CN212039868 U CN 212039868U
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Abstract
The utility model belongs to the field of dilute liquid thickening (filtering) equipment, in particular to a micro-differential thickening or filtering device and a multi-stage combined thickening or filtering device, the thickening and filtering device adopts a filter material to divide dilute liquid into two parts of concentrated liquid and clear liquid and then to be discharged through a conduit respectively, the dilute liquid and the concentrated liquid in the device are positioned at the same side of the filter material, the concentrated liquid is formed by the dilute liquid through shrinking gradually, a clapboard is used for supporting the filter material and has a baffle function, in order to keep the continuity and the stability of the thickening process, a liquid level baffle is further adopted to control the flow of the dilute liquid to be matched with the capability of the device, the liquid level at two sides of the filter material is controlled to be matched with the capability of the filter material, in order to meet the requirements of different thickening (filtering) degrees, a multi-stage combined device is further formed by two or more devices, the product of the former device of the latter device is used as a raw material and is connected into a whole by the conduit in sequence, the thickening degree of the device can be achieved.
Description
Technical Field
The utility model belongs to the field of dilute liquid thickening (filtering) equipment, in particular to micro-differential thickening or filtering equipment and a multistage combined thickening or filtering device.
Background
The dilute liquid thickening (filtering) equipment belongs to the special equipment for liquid-solid separation, and has wide application in the fields of coal, petrochemical industry, pharmacy, environmental protection and the like. The existing thickening (filtering) equipment has the characteristics of large pressure difference in the separation process and intermittent working, and particularly has the defects of high energy consumption, low output ratio and the like under the condition of large liquid-solid ratio.
SUMMERY OF THE UTILITY MODEL
In order to solve the problem of the prior dilute liquid thickening (filtering) equipment, the utility model provides a thickening or filtering equipment and a multistage combined thickening or filtering device. The utility model discloses a poor dilute solution of minute-pressure thickens (filters) equipment is through specifically setting up the liquid level working height in each groove and utilizing the less difference in height between each groove liquid level, thereby overcomes the resistance of filter media and runner, and then realizes thickening (filtering) operation. The equipment operates at normal pressure, can work continuously, and has simple and visual operation parts.
In order to solve the technical problem, the utility model discloses a technical scheme be: a thickening or filtering device comprises a splicing body which is composed of a plurality of shells with certain structures, a concentrated liquid tank, a clear liquid tank, a dilute liquid tank, a liquid level baffle, a clapboard, a filter material and a conduit in sequence; wherein, the peripheral end of the filter material is connected with the clapboard, and the formed connecting body is arranged in the shell; the liquid level baffles are respectively arranged in at least one of the dilute liquid tank, the concentrated liquid tank and the clear liquid tank; working medium inlets are respectively arranged on the tank walls of one side of the liquid level baffles in the concentrated liquid tank and the clear liquid tank, working medium outlets are respectively arranged on the tank walls of the other side of the liquid level baffles in the dilute liquid tank, the tank wall of one side of the liquid level baffle in the dilute liquid tank is provided with a working medium inlet and a working medium outlet, and the tank wall of the other side of the liquid level baffle is provided with; in the cavity at two sides formed by the division of the filter material in the shell, the upper part of one side of the cavity is communicated with the working medium outlet of the dilute liquid tank through a guide pipe, the lower part of the cavity at the other side is communicated with the working medium inlet of the concentrated liquid tank through a guide pipe, the lower part of the cavity at the other side is communicated with the working medium inlet of the clear liquid tank through a guide pipe, and the two sides of the filter material are communicated through a filter gap;
the setting height of the top end of the liquid level baffle in the dilute liquid tank is not lower than the setting height of the top ends of the liquid level baffles in the concentrated liquid tank and the clear liquid tank, and has a certain distance; the setting height of the top end of the liquid level baffle in the clear liquid tank is not lower than that of the top end of the liquid level baffle in the concentrated liquid tank, and has a certain distance; the height of the top ends of the liquid level baffles in the dilute liquid tank, the concentrated liquid tank and the clear liquid tank is lower than that of the shell and the tank body where the shell and the tank body are respectively located, and a certain distance is provided.
Furthermore, the connecting body composed of the filter material and the partition board has a plate-shaped appearance of the filter material, and the periphery of the connecting body is connected with the partition board.
Furthermore, the connecting body formed by the filter material and the partition board has the appearance of a tubular filter material and the appearance of a tube plate, and the pipe openings at the two ends of the filter material are respectively connected with the pipe holes on the flower plate-shaped partition board.
Furthermore, the connecting body formed by the filter material and the partition board has the appearance of a cylindrical filter material, the appearance of the partition board connected with the cylindrical filter material is in a tube plate shape, and the tube opening of the filter material is connected with the tube hole of the flower plate-shaped partition board.
Furthermore, the filter material with a certain structure is a mixture of the filter material and the framework.
Furthermore, the height of the top end of the liquid level baffle with the certain structure is adjustable. So as to adjust the height of the top end of the baffle plate when needed until or realize the requirement of continuous differential adjustment.
Further, the conduit with the certain structure is synthesized together with a conveying or stirring device.
The utility model discloses two other technical scheme of protection for with aforementioned utility model's several differential rare fluid of minute pressure thickening (or filter) equipment according to the combination back of grading according to certain rule, use the occasion that has certain requirement to the liquid-solid ratio of rare fluid thickening (or filter) operation product.
The utility model provides a thickening device is united to multistage, including the complex that is no less than two sets of preceding thickening equipment and a plurality of pipe are connected according to the preface, have certain difference in height between each thickening equipment, the thick liquid groove working medium export of higher thickening equipment all link up with the thin liquid groove working medium import connection of lower thickening equipment through the pipe in order, the working medium export in the clear solution groove of each thickening equipment link up through the pipe connection, the overflow mouth of each thin liquid groove link up through the pipe connection, the general working medium business turn over mouth of pipe of thickening device is thin liquid mouth, thick liquid mouth, clear liquid mouth and overflow mouth respectively jointly to multistage.
A multi-stage combined filtering device comprises at least two sets of combined bodies which are sequentially connected by the filtering equipment and a plurality of guide pipes; the filtering equipment rooms have certain height difference, the clear liquid tank working medium outlet of the filtering equipment at a higher position is sequentially communicated with the dilute liquid tank working medium inlet of the filtering equipment at a lower position through a guide pipe, the concentrated liquid tank working medium outlet of the filtering equipment is communicated through a guide pipe, the overflow port of the dilute liquid tank is communicated through a guide pipe, and the working medium inlet and outlet pipe ports of the multi-stage combined filtering device are respectively a dilute liquid port, a concentrated liquid port, a clear liquid port and an overflow port.
Compared with the prior art, the utility model following beneficial effect has: the dilute liquid thickening (filtering) equipment and the multistage combined thickening (filtering) device of the utility model can overcome the flow resistance of the filter material and the conduit and the loss of the falling water head by setting a certain liquid level difference among the dilute liquid working liquid level, the concentrated liquid working liquid level and the clear liquid working liquid level, and can realize the control and matching of the flow of each part in the equipment or the device;
the utility model discloses a differential dilute solution of minute-pressure thickens (filters) equipment and multistage joint thickening (filters) device can divide into plate-type, tubular and three kinds of cartridge according to the geometric characteristics of filter media in it, ordinary pressure, continuous operation system, and equipment structure is simple and clear, and the power consumption is less, and the operation is maintained portably.
Drawings
Fig. 1 is a schematic structural diagram of a plate-type micro-differential pressure dilute liquid thickening (filtering) device.
Fig. 2 is a schematic structural diagram of a tubular micro-differential pressure dilute liquid thickening (filtering) device.
FIG. 3 is a schematic structural diagram of a cartridge type micro-differential pressure dilute liquid thickening (filtering) device.
FIG. 4 is a schematic structural diagram of a multi-stage combined thickening apparatus.
FIG. 5 is a schematic diagram of a multi-stage integrated filter arrangement.
In the figure, 1 is a shell, 2 is a concentrated solution tank, 3 is a clear solution tank, 4 is a dilute solution tank, 5 is a dilute solution baffle, 6 is a partition plate, 7 is a filter material, and 8 is a conduit.
Detailed Description
The utility model provides a thickening or filtration equipment. The thickening or filtering device adopts a filter material to divide dilute liquid into concentrated liquid and clear liquid which are then respectively discharged through a conduit, wherein the dilute liquid and the concentrated liquid in the filter material are positioned at the same side of the filter material, the concentrated liquid is formed by gradually shrinking the dilute liquid, and in order to meet the requirements of different operation amounts, the filter material is further divided into three types, namely a plate type, a tube type and a barrel type, wherein the plate type is suitable for smaller occasions, and the barrel type is suitable for larger occasions, and the tube type is arranged between the plate type, the tube type and the barrel type.
As shown in fig. 1, the utility model discloses a technical scheme of protection: plate-type micro-differential pressure dilute liquid thickening (or filtering) equipment: comprises a splicing body which is composed of a plurality of shells 1, a concentrated solution tank 2, a clear solution tank 3, a dilute solution tank 4, a liquid level baffle 5, a clapboard 6, a filter material 7 and a conduit 8 which are all in a certain structure in sequence; wherein, the peripheral end of the plate-shaped filter material 7 is connected with the clapboard 6, and the formed connecting body is arranged in the shell 1; the liquid level baffle 5 is respectively arranged in at least one dilute liquid tank 4, one concentrated liquid tank 2 and one clear liquid tank 3; working medium inlets are respectively arranged on the tank walls of one side of the liquid level baffles 5 in the concentrated solution tank 2 and the clear solution tank 3, working medium outlets are respectively arranged on the tank wall of the other side of the liquid level baffles, the working medium inlet and the working medium outlet are arranged on the tank wall of one side of the liquid level baffles 5 in the dilute solution tank 4, and overflow ports are arranged on the tank wall of the other side of the liquid level baffles; in a cavity on two sides formed by dividing the shell 1 by a plate-shaped filter material 7, the upper part of one side of the cavity is communicated with a working medium outlet of a dilute liquid tank 4 through a guide pipe 8, the lower part of the cavity on the other side is communicated with a working medium inlet of a concentrated liquid tank 2 through the guide pipe 8, the lower part of the cavity on the other side is communicated with a working medium inlet of a clear liquid tank 3 through the guide pipe 8, and two sides of the filter material 7 are communicated through a filter gap of the filter.
The setting height of the top end of the liquid level baffle 5 in the dilute liquid tank 4 is not lower than the setting height of the top ends of the liquid level baffles 5 in the concentrated liquid tank 2 and the clear liquid tank 3, and has a certain distance; the setting height of the top end of the liquid level baffle 5 in the clear liquid tank 3 is not lower than the setting height of the top end of the liquid level baffle 5 in the concentrated liquid tank 2, and has a certain distance; the height of the top ends of the liquid level baffles 5 in the dilute liquid tank 4, the concentrated liquid tank 2 and the clear liquid tank 3 is lower than that of the shell 1 and the respective tank body, and a certain distance is provided.
The working principle of the device is as follows:
the dilute liquid is injected into the dilute liquid tank 4 from the liquid inlet, and then is transferred into the shell 1 (one side of the plate-shaped filter material) through the conduit 8, the clear liquid (on the other side of the plate-shaped filter material) enters the clear liquid tank 3 through the conduit 8 under the separation action of the filter material, and the concentrated liquid enters the concentrated liquid tank 2 through the conduit 8; in the process, under the action of the liquid level baffles 5 in the concentrated liquid tank 2 and the clear liquid tank 3, the outflow of the clear liquid and the concentrated liquid needs to cross the corresponding liquid level baffles 5, so that the working liquid level of the clear liquid and the concentrated liquid has certain stability, and when the liquid level baffles 5 in the dilute liquid tank 4 and the partition plates 6 in the shell are higher than the liquid level baffles 5 in the concentrated liquid tank 2 and the clear liquid tank 3 by a certain height, the pushing action of the liquid level difference can be utilized, and the continuity and the stability of the thickening operation process are realized; meanwhile, the effect of adjusting the output ratio of the concentrated solution and the clear solution can be achieved by setting the height difference between the liquid level baffles in the concentrated solution tank 2 and the clear solution tank 3.
As shown in fig. 2, the utility model discloses another technical scheme of protection: pipe type micro-differential pressure dilute liquid thickening (or filtering) equipment: comprises a splicing body which is composed of a plurality of shells 1, a concentrated solution tank 2, a clear solution tank 3, a dilute solution tank 4, a liquid level baffle 5, a clapboard 6, a filter material 7 and a conduit 8 which are all in a certain structure in sequence; wherein, two ends of the tubular filter material 7 are respectively connected with the tube plate-shaped clapboard 6, and the formed connecting body is arranged in the shell 1; the liquid level baffle 5 is respectively arranged in at least one dilute liquid tank 4, one concentrated liquid tank 2 and one clear liquid tank 3; working medium inlets are respectively arranged on the tank walls of one side of the liquid level baffles 5 in the concentrated solution tank 2 and the clear solution tank 3, working medium outlets are respectively arranged on the tank wall of the other side of the liquid level baffles, the working medium inlet and the working medium outlet are arranged on the tank wall of one side of the liquid level baffles 5 in the dilute solution tank 4, and overflow ports are arranged on the tank wall of the other side of the liquid level baffles;
in a cavity on two sides formed by dividing the shell 1 by a tubular filter material 7, the upper part of the inner side of the tubular filter material is communicated with a working medium outlet of a dilute liquid tank 4 through a guide pipe 8, the lower part of the inner side of the tubular filter material is communicated with a working medium inlet of a concentrated liquid tank 2 through the guide pipe 8, the lower part of the cavity on the outer side is communicated with a working medium inlet of a clear liquid tank 3 through the guide pipe 8, and two sides of the tubular filter material 7 are communicated through a filter gap of the;
the setting height of the top end of the liquid level baffle 5 in the dilute liquid tank 4 is not lower than the setting height of the top ends of the liquid level baffles 5 in the concentrated liquid tank 2 and the clear liquid tank 3, and has a certain distance; the setting height of the top end of the liquid level baffle 5 in the clear liquid tank 3 is not lower than the setting height of the top end of the liquid level baffle 5 in the concentrated liquid tank 2, and has a certain distance; the height of the top ends of the liquid level baffles 5 in the dilute liquid tank 4, the concentrated liquid tank 2 and the clear liquid tank 3 is lower than that of the shell 1 and the respective tank body, and a certain distance is provided.
The working principle of the pipe type micro-differential pressure dilute liquid thickening (or filtering) equipment is as follows:
the dilute liquid is injected into the dilute liquid tank 4 from the liquid inlet, and then is transferred into the shell 1 (the inner side of the tubular filter material) through the conduit 8, the clear liquid (at the outer side of the tubular filter material) enters the clear liquid tank 3 through the conduit 8 under the separation action of the filter material, and the concentrated liquid enters the concentrated liquid tank 2 through the conduit 8; in the process, under the action of the liquid level baffles 5 in the concentrated liquid tank 2 and the clear liquid tank 3, the outflow of the clear liquid and the concentrated liquid needs to cross the corresponding liquid level baffles 5, so that the working liquid levels of the clear liquid and the concentrated liquid have certain stability, and when the liquid level baffles 5 in the dilute liquid tank 4 and the partition plates in the shell are higher than the liquid level baffles 5 in the concentrated liquid tank 2 and the clear liquid tank 3 by a certain height, the pushing action of the liquid level difference can be utilized, and the continuity and the stability of the thickening operation process are realized; meanwhile, the effect of adjusting the output ratio of the concentrated solution and the clear solution can be achieved by setting the height difference between the liquid level baffles in the concentrated solution tank 2 and the clear solution tank 3.
As shown in fig. 3, the present invention provides a further technical solution: cartridge-type micro-differential pressure dilute liquid thickening (or filtering) equipment: comprises a splicing body which is composed of a plurality of shells 1, a concentrated solution tank 2, a clear solution tank 3, a dilute solution tank 4, a liquid level baffle 5, a clapboard 6, a filter material 7 and a conduit 8 which are all in a certain structure in sequence; wherein, the port of the cylindrical filter material 7 is connected with the tube plate-shaped clapboard 6, and the formed connecting body is arranged in the shell 1; the liquid level baffle 5 is respectively arranged in at least one dilute liquid tank 4, one concentrated liquid tank 2 and one clear liquid tank 3; working medium inlets are respectively arranged on the tank walls of one side of the liquid level baffles 5 in the concentrated solution tank 2 and the clear solution tank 3, working medium outlets are respectively arranged on the tank wall of the other side of the liquid level baffles, the working medium inlet and the working medium outlet are arranged on the tank wall of one side of the liquid level baffles 5 in the dilute solution tank 4, and overflow ports are arranged on the tank wall of the other side of the liquid level baffles;
in a cavity on two sides formed by the division of a tubular filter material 7 in the shell 1, the upper part of the inner side of the tubular filter material is communicated with a working medium inlet of the clear liquid tank 3 through a guide pipe 8, the upper part of the outer side of the tubular filter material is communicated with a working medium outlet of the dilute liquid tank 4 through the guide pipe 8, the lower part of the outer side of the tubular filter material is communicated with a working medium inlet of the concentrated liquid tank 2 through the guide pipe 8, and two sides of the tubular filter material 7 are communicated through a filter;
the setting height of the top end of the liquid level baffle 5 in the dilute liquid tank 4 is not lower than the setting height of the top ends of the liquid level baffles 5 in the concentrated liquid tank 2 and the clear liquid tank 3, and has a certain distance; the setting height of the top end of the liquid level baffle 5 in the clear liquid tank 3 is not lower than the setting height of the top end of the liquid level baffle 5 in the concentrated liquid tank 2, and has a certain distance; the height of the top ends of the liquid level baffles 5 in the dilute liquid tank 4, the concentrated liquid tank 2 and the clear liquid tank 3 is lower than that of the shell 1 and the respective tank body, and a certain distance is provided.
The working principle of the cartridge type micro-differential pressure dilute liquid thickening (or filtering) equipment is as follows:
the dilute liquid is injected into the dilute liquid tank 4 from the liquid inlet, and then is transferred into the shell 1 (the outer side of the cylindrical filter material) through the conduit 8, the clear liquid (at the inner side of the tubular filter material) enters the clear liquid tank 3 through the conduit 8 under the separation action of the filter material, and the concentrated liquid enters the concentrated liquid tank 2 through the conduit 8; in the process, under the action of the liquid level baffles 5 in the concentrated liquid tank 2 and the clear liquid tank 3, the outflow of the clear liquid and the concentrated liquid needs to cross the corresponding liquid level baffles 5, so that the working liquid levels of the clear liquid and the concentrated liquid have certain stability, and when the liquid level baffles 5 in the dilute liquid tank 4 and the partition plates in the shell are higher than the liquid level baffles 5 in the concentrated liquid tank 2 and the clear liquid tank 3 by a certain height, the pushing action of the liquid level difference can be utilized, and the continuity and the stability of the thickening operation process are realized; meanwhile, the effect of adjusting the output ratio of the concentrated solution and the clear solution can be achieved by setting the height difference between the liquid level baffles in the concentrated solution tank 2 and the clear solution tank 3.
Three basic application forms of the micro-differential pressure dilute liquid thickening (filtering) device have been briefly described and illustrated. The utility model discloses mainly utilize the less liquid level difference of yardstick to realize equipment at the continuous operation of ordinary pressure, to the characteristic and the operation requirement of different working mediums, always can realize the continuous normal work of equipment through the setting of liquid level difference. The whole equipment is simple in structure and low in maintenance cost.
As shown in fig. 3 and 4, the following is a description of an embodiment of the multistage combined thickening and filtering apparatus.
The multistage combined thickening and filtering device is a combination body formed by sequentially connecting at least two thickening and filtering devices and a plurality of guide pipes 8, wherein the thickening devices are arranged according to a certain height difference (as shown in h2 and h1 in the figure), working medium outlets of a concentrated solution tank 2 on a higher device are sequentially and sequentially communicated with working medium inlets of a dilute solution tank 4 on a next higher device through the guide pipes 8, working medium outlets of a clear solution tank 3 on each device are communicated through the guide pipes 8, and overflow ports of the dilute solution tanks 4 are communicated through the guide pipes 8; the working medium inlet and outlet pipe orifices of the multi-stage combined thickening and filtering device are respectively a dilute liquid orifice X, a concentrated liquid orifice N, a clear liquid orifice Q and a overflowing liquid orifice Y.
The working principle of the multi-stage combined thickening device is as follows:
the multistage combined thickening device is designed for improving the thickening degree and the filtering degree, and the working principle of the multistage combined thickening device lies in that: and the concentrated liquid (product) discharged from the former thickening equipment is used as the dilute liquid (raw material) of the latter thickening equipment for thickening operation in turn until the aim of meeting the designed consistency is achieved.
The duct described above is further provided with a structure having a transport capability or a stirring capability, if necessary, so as not to cause clogging of the duct.
The thickening and filtering equipment and the combined thickening and filtering device thereof have loose requirements on the operating environment, and have the characteristics of compact structure, lower early construction cost and simple and easy operation and maintenance; when reasonably configured, the requirement of continuous and stable work can be met;
although the embodiments of the present invention have been described in detail, the present invention is not limited to the above embodiments, and various changes can be made without departing from the spirit of the present invention within the knowledge of those skilled in the art.
Claims (9)
1. A micro-differential pressure thickening or filtering device is characterized by comprising a splicing body which is composed of a plurality of shells (1) with certain structures, a concentrated liquid groove (2), a clear liquid groove (3), a dilute liquid groove (4), a liquid level baffle (5), a partition plate (6), a filter material (7) and a conduit (8) in sequence; wherein, the peripheral end of the filter material (7) is connected with the clapboard (6), and the formed connecting body is arranged in the shell (1); a plurality of liquid level baffles (5) are respectively arranged in at least one dilute liquid tank (4), one concentrated liquid tank (2) and one clear liquid tank (3); working medium inlets are respectively arranged on the tank wall of one side of the liquid level baffle (5) in the concentrated solution tank (2) and the clear solution tank (3), working medium outlets are respectively arranged on the tank wall of the other side of the liquid level baffle, the working medium inlet and the working medium outlet are arranged on the tank wall of one side of the liquid level baffle (5) in the dilute solution tank (4), and an overflow port is arranged on the tank wall of the other side of the liquid level baffle; in a cavity on two sides formed by dividing the shell (1) by a filter material (7), the upper part of one side of the cavity is communicated with a working medium outlet of the dilute liquid tank (4) through a guide pipe (8), the lower part of the cavity is communicated with a working medium inlet of the concentrated liquid tank (2) through the guide pipe (8), the lower part of the cavity on the other side is communicated with a working medium inlet of the clear liquid tank (3) through the guide pipe (8), and the two sides of the filter material (7) are communicated with each other through a filter gap of the filter material (7);
the setting height of the top end of the liquid level baffle (5) in the dilute liquid tank (4) is not lower than the setting height of the top ends of the liquid level baffles (5) in the concentrated liquid tank (2) and the clear liquid tank (3), and a certain distance is provided; the setting height of the top end of the liquid level baffle (5) in the clear liquid tank (3) is not lower than that of the top end of the liquid level baffle (5) in the concentrated liquid tank (2), and a certain distance is provided; the top ends of the liquid level baffles (5) in the dilute liquid tank (4), the concentrated liquid tank (2) and the clear liquid tank (3) are all lower than the shell (1) and the respective tank bodies and have a certain distance.
2. A micro-differential pressure thickening or filtering apparatus according to claim 1, wherein: the connecting body composed of the filter material (7) and the clapboard (6) has the appearance of a plate-shaped inner filter material (7), and the periphery of the inner filter material is connected with the clapboard (6).
3. A micro-differential pressure thickening or filtering apparatus according to claim 1, wherein: the connecting body formed by the filter material (7) and the partition board (6) is characterized in that the appearance of the filter material (7) in the connecting body is tubular, the appearance of the partition board (6) is tube plate-shaped, and pipe orifices at two ends of the filter material (7) are respectively connected with pipe orifices on the flower plate-shaped partition board (6).
4. A micro-differential pressure thickening or filtering apparatus according to claim 1, wherein: the connecting body formed by the filter material (7) and the partition board (6) has the appearance that the filter material (7) is cylindrical, the partition board (6) connected with the filter material is tubular-plate-shaped, and the tubular opening of the filter material (7) is connected with the tubular hole of the flower-plate-shaped partition board (6).
5. A micro-differential pressure thickening or filtering apparatus according to claim 1, wherein: the filter material (7) with a certain structure is a mixture of the filter material and the framework.
6. A micro-differential pressure thickening or filtering apparatus according to claim 1, wherein: the height of the top end of the liquid level baffle (5) with a certain structure is adjustable.
7. A micro-differential pressure thickening or filtering apparatus according to claim 1, wherein: the conduit (8) with a certain structure is synthesized together with a conveying or stirring device.
8. A multi-stage combined thickening device is characterized in that: the device comprises at least two sets of combination bodies which are sequentially connected by the thickening equipment as claimed in any one of claims 1 to 7 and a plurality of guide pipes, wherein a certain height difference exists between the thickening equipment, the working medium outlet of the concentrated solution tank of the higher thickening equipment is sequentially communicated with the working medium inlet of the dilute solution tank of the lower thickening equipment through the guide pipes, the working medium outlet of the clear solution tank of each thickening equipment is communicated through the guide pipes, the overflow port of each dilute solution tank is communicated through the guide pipes, and the working medium inlet and outlet orifices of the overall multistage combination thickening device are respectively a dilute solution port, a concentrated solution port, a clear solution port and an overflow port.
9. A multi-stage combined filter device, comprising: a combination comprising no less than two sets of the filtering apparatus of any one of claims 1 to 7 and a plurality of conduits connected in series; the filtering equipment rooms have certain height difference, the clear liquid tank working medium outlet of the filtering equipment at a higher position is sequentially communicated with the dilute liquid tank working medium inlet of the filtering equipment at a lower position through a guide pipe, the concentrated liquid tank working medium outlet of the filtering equipment is communicated through a guide pipe, the overflow port of the dilute liquid tank is communicated through a guide pipe, and the working medium inlet and outlet pipe ports of the multi-stage combined filtering device are respectively a dilute liquid port, a concentrated liquid port, a clear liquid port and an overflow port.
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111151136A (en) * | 2020-03-11 | 2020-05-15 | 陈以原 | Micro-differential pressure thickening or filtering equipment and multi-stage combined thickening or filtering device |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111151136A (en) * | 2020-03-11 | 2020-05-15 | 陈以原 | Micro-differential pressure thickening or filtering equipment and multi-stage combined thickening or filtering device |
| CN111151136B (en) * | 2020-03-11 | 2024-04-09 | 陈以原 | Micro-differential pressure thickening or filtering equipment and multi-stage combined thickening or filtering device |
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