CN211886859U - Immersion type continuous production device for defluorination filter material - Google Patents
Immersion type continuous production device for defluorination filter material Download PDFInfo
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- CN211886859U CN211886859U CN202020306083.8U CN202020306083U CN211886859U CN 211886859 U CN211886859 U CN 211886859U CN 202020306083 U CN202020306083 U CN 202020306083U CN 211886859 U CN211886859 U CN 211886859U
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Abstract
The utility model discloses a continuous production device of soaking type defluorination filter material, which comprises a reaction chamber, an acid liquid tank and an alkali liquid tank; the reaction chamber is divided into a plurality of reaction tanks provided with feed openings; the liquid outlets of the acid liquid tank and the alkali liquid tank are respectively connected with an input communicating pipe, the input communicating pipe is connected with the liquid inlet of the first reaction tank through a lift pump, and the liquid outlet of the first reaction tank is communicated with the second reaction tank through a communicating pipe; the liquid outlet of the second reaction tank is communicated with the third reaction tank through a communicating pipe, the liquid outlet of the third reaction tank is communicated with the fourth reaction tank through a communicating pipe, the liquid outlet of the fourth reaction tank is connected with an output communicating pipe through a communicating pipe, and the output communicating pipe is respectively connected with the circulating liquid inlet of the acid liquid tank and the circulating liquid inlet of the alkali liquid tank. Compare with the mode of a present batch of material, a batch of acid, a batch of alkali, the utility model discloses reducible equipment investment effectively utilizes reaction time, improves reaction efficiency and production efficiency.
Description
Technical Field
The utility model belongs to the technical field of water treatment facilities, a soak formula defluorination filter material continuous production device is related to.
Background
The soaking type defluorination filter material is a common water treatment material, and the production premise is that the raw materials and an acid-base solution react in sequence, and the processes of feeding, adding acid-base, discharging and the like are required to be repeated continuously. Therefore, a reaction tank is required to realize the process. The traditional chemical reaction kettle has the advantages of single form, large occupied area and large energy consumption, adopts a production mode of one batch of acid and one batch of alkali, and cannot utilize the reaction waiting time in each production process.
Disclosure of Invention
The technical problem solved by the utility model is to provide a soak formula defluorination filter material continuous production device, through setting up a plurality of reaction tanks, combine reaction sequence control valve's control, realize incessant reaction.
The utility model discloses a realize through following technical scheme:
a continuous production device of soaking type defluorination filter material comprises a reaction chamber, an acid liquid tank and an alkali liquid tank; the reaction chamber is divided into a plurality of reaction tanks provided with feed openings; the liquid outlets of the acid liquid tank and the alkali liquid tank are respectively connected with an input communicating pipe, the input communicating pipe is connected with the liquid inlet of the first reaction tank through a lift pump, and the liquid outlet of the first reaction tank is communicated with the second reaction tank through a communicating pipe; the liquid outlet of the second reaction tank is communicated with the third reaction tank through a communicating pipe, the liquid outlet of the third reaction tank is communicated with the fourth reaction tank through a communicating pipe, the liquid outlet of the fourth reaction tank is connected with an output communicating pipe through a communicating pipe, and the output communicating pipe is respectively connected with the circulating liquid inlet of the acid liquid tank and the circulating liquid inlet of the alkali liquid tank.
The side of the reaction chamber is provided with an operation chamber, the acid liquor tank and the alkali liquor tank are arranged in the operation chamber in parallel, and the lift pump is arranged at the side of the acid liquor tank.
And a reaction sequence control valve is arranged at the liquid outlet of the reaction tank or on a communicating pipe connected with the liquid outlet, the reaction sequence control valve is closed when the reaction of the previous reaction tank is carried out, the reaction sequence control valve is opened after the reaction is finished, and acid liquor or alkali liquor enters the next reaction tank.
The reaction sequence control valves of the reaction tanks are periodically closed or opened:
the first stage is as follows: all reaction sequence control valves are closed, and the first reaction tank is fed;
and a second stage: all reaction sequence control valves are closed; adding acid liquor into the first reaction tank, and feeding the acid liquor into the second reaction tank;
and a third stage: opening a first reaction sequence control valve, closing the other reaction sequence control valves, closing the acid liquor in the first reaction tank after entering a second reaction tank, and adding alkali after the acid in the first reaction tank is drained; feeding in a third reaction tank;
a fourth stage: opening a second reaction sequence control valve, closing the other reaction sequence control valves, and discharging the acid liquor in the second reaction tank into a third reaction tank; after the acid liquor in the second reaction tank is drained, the first reaction sequence control valve is opened, the second reaction sequence control valve is closed, and the alkali liquor in the first reaction tank enters the second reaction tank; discharging in the first reaction tank, and feeding in the fourth reaction tank;
the fifth stage: the third reaction sequence control valve is opened, the other reaction sequence control valves are closed, and acid liquor in the third reaction tank is discharged into the fourth reaction tank; after the acid liquor in the third reaction tank is drained, the second reaction sequence control valve is opened, the third reaction sequence control valve is closed, and the alkali liquor in the second reaction tank enters the third reaction tank; discharging the material in the second reaction tank, and feeding the material in the first reaction tank, wherein one period is completed.
The reaction tanks are arranged in a straight line;
or the reaction tanks are distributed in two rows, the first reaction tank and the second reaction tank are arranged in one row, the third reaction tank and the fourth reaction tank are arranged in one row, and the first reaction tank and the fourth reaction tank are arranged side by side; the input communicating pipe and the output communicating pipe are arranged in parallel.
Compared with the prior art, the utility model discloses following profitable technological effect has:
the utility model provides a continuous production device of soaking type defluorination filter material, which divides a reaction chamber into a plurality of reaction tanks, wherein the liquid outlet of the previous reaction tank is communicated with the next reaction tank, thus realizing the combination of a single unit and the whole body, and each reaction tank enters acid liquid or alkali liquid according to the reaction progress degree on the whole, and then the acid liquid or the alkali liquid after the reaction is finished is discharged into the next reaction tank, and finally enters an acid liquid tank and an alkali liquid tank for recycling; the acid reaction and the alkali reaction of each unit have no terminal, no reaction interval exists, and the uninterrupted reaction of the reactor can be realized only by controlling the opening or closing of the valve through the reaction sequence. Compared with the existing mode of one batch of acid and one batch of alkali, the method has the advantages of reducing equipment investment, effectively utilizing reaction time and improving reaction efficiency and production efficiency.
Drawings
Fig. 1 is a schematic structural view of the present invention;
FIG. 2 is a schematic diagram of the sequential reaction of each reaction tank
Wherein, 1 is a liquid inlet, 2 is a feed opening, 3 is a communicating pipe, 4 is an alkali liquor tank, 5 is an acid liquor tank, and 6 is a lift pump.
Detailed Description
The present invention will now be described in further detail with reference to the attached drawings, which are provided for purposes of illustration and not limitation.
Referring to fig. 1, a continuous production device of soaking type defluorination filter material comprises a reaction chamber, an acid liquid tank and an alkali liquid tank; the reaction chamber is divided into a plurality of reaction tanks provided with feed openings; the liquid outlets of the acid liquid tank and the alkali liquid tank are respectively connected with an input communicating pipe, the input communicating pipe is connected with the liquid inlet of the first reaction tank through a lift pump, and the liquid outlet of the first reaction tank is communicated with the second reaction tank through a communicating pipe; the liquid outlet of the second reaction tank is communicated with the third reaction tank through a communicating pipe, the liquid outlet of the third reaction tank is communicated with the fourth reaction tank through a communicating pipe, the liquid outlet of the fourth reaction tank is connected with an output communicating pipe through a communicating pipe, and the output communicating pipe is respectively connected with the circulating liquid inlet of the acid liquid tank and the circulating liquid inlet of the alkali liquid tank.
In order to facilitate operation and management, an operation chamber is arranged beside the reaction chamber, an acid solution tank and an alkali solution tank are arranged in the operation chamber in parallel, and a lift pump is arranged beside the acid solution tank.
In the arrangement, it may be arranged according to space or reaction conditions:
the reaction tanks are arranged in a straight line;
or the reaction tanks are distributed in two rows, the first reaction tank and the second reaction tank are arranged in one row, the third reaction tank and the fourth reaction tank are arranged in one row, and the first reaction tank and the fourth reaction tank are arranged side by side; the input communicating pipe and the output communicating pipe are arranged in parallel.
The liquid outlet of the reaction tank or a communicating pipe connected with the liquid outlet is provided with a reaction sequence control valve, the reaction sequence control valve is closed when the reaction of the previous reaction tank is carried out, the reaction sequence control valve is opened after the reaction is finished, acid liquor or alkali liquor enters the next reaction tank, and each reaction tank continuously reacts.
Specifically, each group of each reaction chamber device is divided into 4 reaction cells, which are respectively counted as cells 1, 2, 3, and 4 from the top left corner in the counterclockwise direction, and the reaction flow is shown in fig. 2 by taking the reaction cycle of the cell 1 as an example:
the first stage is as follows: feeding in a first tank;
and a second stage: adding acid into the first tank, and feeding into the second tank;
and a third stage: feeding acid discharged from the first tank into a second tank, feeding in a third tank, and adding alkali when the acid discharged from the first tank is exhausted;
a fourth stage: feeding in the fourth tank, discharging acid in the second tank into the third tank, discharging alkali in the first tank into the second tank when the acid in the second tank is discharged completely, and discharging in the first tank.
The fifth stage: feeding the first pool, discharging the third pool acid into the fourth pool, discharging the second pool alkali into the third pool when the third pool acid is discharged completely, discharging the second pool when the third pool acid is discharged completely, and finishing a reaction period.
Correspondingly, the reaction sequence control valve of each reaction tank is periodically closed or opened:
the first stage is as follows: all reaction sequence control valves are closed, and the first reaction tank is fed;
and a second stage: all reaction sequence control valves are closed; adding acid liquor into the first reaction tank, and feeding the acid liquor into the second reaction tank;
and a third stage: opening a first reaction sequence control valve, closing the other reaction sequence control valves, closing the acid liquor in the first reaction tank after entering a second reaction tank, and adding alkali after the acid in the first reaction tank is drained; feeding in a third reaction tank;
a fourth stage: opening a second reaction sequence control valve, closing the other reaction sequence control valves, and discharging the acid liquor in the second reaction tank into a third reaction tank; after the acid liquor in the second reaction tank is drained, the first reaction sequence control valve is opened, the second reaction sequence control valve is closed, and the alkali liquor in the first reaction tank enters the second reaction tank; discharging in the first reaction tank, and feeding in the fourth reaction tank;
the fifth stage: the third reaction sequence control valve is opened, the other reaction sequence control valves are closed, and acid liquor in the third reaction tank is discharged into the fourth reaction tank; after the acid liquor in the third reaction tank is drained, the second reaction sequence control valve is opened, the third reaction sequence control valve is closed, and the alkali liquor in the second reaction tank enters the third reaction tank; discharging the material in the second reaction tank, and feeding the material in the first reaction tank, wherein one period is completed.
Therefore, the utility model discloses be different from traditional production facility, separate each reaction tank, through the sequence control of acidizing fluid or alkali lye, realized the continuous uninterrupted production of soaking formula defluorination filter material in the reacting chamber.
The embodiments given above are preferred examples for implementing the present invention, and the present invention is not limited to the above-described embodiments. Any non-essential addition and replacement made by the technical features of the technical solution of the present invention by those skilled in the art all belong to the protection scope of the present invention.
Claims (5)
1. A continuous production device of soaking type defluorination filter material is characterized by comprising a reaction chamber, an acid liquid tank and an alkali liquid tank; the reaction chamber is divided into a plurality of reaction tanks provided with feed openings; the liquid outlets of the acid liquid tank and the alkali liquid tank are respectively connected with an input communicating pipe, the input communicating pipe is connected with the liquid inlet of the first reaction tank through a lift pump, and the liquid outlet of the first reaction tank is communicated with the second reaction tank through a communicating pipe; the liquid outlet of the second reaction tank is communicated with the third reaction tank through a communicating pipe, the liquid outlet of the third reaction tank is communicated with the fourth reaction tank through a communicating pipe, the liquid outlet of the fourth reaction tank is connected with an output communicating pipe through a communicating pipe, and the output communicating pipe is respectively connected with the circulating liquid inlet of the acid liquid tank and the circulating liquid inlet of the alkali liquid tank.
2. The apparatus for continuously producing immersed defluorination filtering material as claimed in claim 1, wherein an operation chamber is provided beside said reaction chamber, an acid solution tank and an alkali solution tank are provided in parallel in the operation chamber, and a lift pump is provided beside the acid solution tank.
3. The continuous production apparatus for the immersed defluorination filtering material as set forth in claim 1, wherein a reaction sequence control valve is provided at the liquid outlet of said reaction tank or on a communicating pipe connected to the liquid outlet, the reaction sequence control valve is closed when the reaction of the previous reaction tank is proceeding, the reaction sequence control valve is opened after the reaction is completed, and the acid solution or alkali solution is fed into the next reaction tank.
4. The continuous production device of the immersed defluorination filtering material as claimed in claim 1, wherein the reaction sequence control valves of each reaction tank are periodically closed or opened:
the first stage is as follows: all reaction sequence control valves are closed, and the first reaction tank is fed;
and a second stage: all reaction sequence control valves are closed; adding acid liquor into the first reaction tank, and feeding the acid liquor into the second reaction tank;
and a third stage: opening a first reaction sequence control valve, closing the other reaction sequence control valves, closing the acid liquor in the first reaction tank after entering a second reaction tank, and adding alkali after the acid in the first reaction tank is drained; feeding in a third reaction tank;
a fourth stage: opening a second reaction sequence control valve, closing the other reaction sequence control valves, and discharging the acid liquor in the second reaction tank into a third reaction tank; after the acid liquor in the second reaction tank is drained, the first reaction sequence control valve is opened, the second reaction sequence control valve is closed, and the alkali liquor in the first reaction tank enters the second reaction tank; discharging in the first reaction tank, and feeding in the fourth reaction tank;
the fifth stage: the third reaction sequence control valve is opened, the other reaction sequence control valves are closed, and acid liquor in the third reaction tank is discharged into the fourth reaction tank; after the acid liquor in the third reaction tank is drained, the second reaction sequence control valve is opened, the third reaction sequence control valve is closed, and the alkali liquor in the second reaction tank enters the third reaction tank; discharging the material in the second reaction tank, and feeding the material in the first reaction tank, wherein one period is completed.
5. The continuous production apparatus of immersed defluorination filtering material as set forth in claim 1, wherein said reaction cells are arranged in a line;
or the reaction tanks are distributed in two rows, the first reaction tank and the second reaction tank are arranged in one row, the third reaction tank and the fourth reaction tank are arranged in one row, and the first reaction tank and the fourth reaction tank are arranged side by side; the input communicating pipe and the output communicating pipe are arranged in parallel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020306083.8U CN211886859U (en) | 2020-03-13 | 2020-03-13 | Immersion type continuous production device for defluorination filter material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020306083.8U CN211886859U (en) | 2020-03-13 | 2020-03-13 | Immersion type continuous production device for defluorination filter material |
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| Publication Number | Publication Date |
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| CN211886859U true CN211886859U (en) | 2020-11-10 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN202020306083.8U Active CN211886859U (en) | 2020-03-13 | 2020-03-13 | Immersion type continuous production device for defluorination filter material |
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| CN (1) | CN211886859U (en) |
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- 2020-03-13 CN CN202020306083.8U patent/CN211886859U/en active Active
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