CN220467666U - Continuous flow electrochemical reactor - Google Patents
Continuous flow electrochemical reactor Download PDFInfo
- Publication number
- CN220467666U CN220467666U CN202321957850.1U CN202321957850U CN220467666U CN 220467666 U CN220467666 U CN 220467666U CN 202321957850 U CN202321957850 U CN 202321957850U CN 220467666 U CN220467666 U CN 220467666U
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- reactor
- inner core
- sewage
- continuous flow
- electrode
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- 239000010865 sewage Substances 0.000 claims abstract description 62
- 230000002572 peristaltic effect Effects 0.000 claims abstract description 15
- 239000004020 conductor Substances 0.000 claims description 25
- 230000037431 insertion Effects 0.000 claims description 15
- 238000003780 insertion Methods 0.000 claims description 15
- 238000009434 installation Methods 0.000 claims description 3
- 230000005611 electricity Effects 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 10
- 239000003344 environmental pollutant Substances 0.000 abstract description 3
- 231100000719 pollutant Toxicity 0.000 abstract description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 238000006056 electrooxidation reaction Methods 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
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- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The utility model belongs to the technical field of electrochemical water treatment, in particular to a continuous flow electrochemical reactor, which comprises a peristaltic pump, a sewage conveying pipe, a reactor shell and two reactor inner cores; the two reactor cores are mutually attached to form a reactor core whole, the sewage passing grooves of the two reactor cores are combined to form a sewage passing space, and the bottom surface of each sewage passing groove of each reactor core is respectively provided with an electrode. According to the utility model, through the matched arrangement of the peristaltic pump, the sewage conveying pipe, the reactor shell and the two reactor cores provided with the electrodes, continuous flow can be used for replacing intermittent flow, pollutants can be directly removed from the continuous flow, water quality is optimized, the treated water quantity can be greatly increased, and the occupied area is saved; when different treatment requirements are met, the inner core of the reactor can be pulled out from the reactor shell, the corresponding electrode is replaced and then placed in the reactor shell again, and the reactor is convenient to use and high in applicability.
Description
Technical Field
The utility model belongs to the technical field of electrochemical water treatment, and particularly relates to a continuous flow electrochemical reactor.
Background
The reactor currently used in conventional electrochemical water treatment technology is a batch flow reactor. The batch flow reactor has a limited amount of treated water and a long treatment time. Especially in the case of wastewater treatment with a large amount of water, the throughput of the batch flow reactor is low. In addition, the footprint of the batch flow reactor is typically relatively large.
Disclosure of Invention
In view of the above, it is an object of the present utility model to provide a continuous flow electrochemical reactor.
The aim of the utility model is realized by the following technical scheme:
a continuous flow electrochemical reactor comprises a peristaltic pump, a sewage conveying pipe, a reactor shell and two reactor inner cores;
a sewage passing groove is formed in one side surface of each reactor inner core, the two reactor inner cores are mutually attached to form a reactor inner core whole, the sewage passing grooves of the two reactor inner cores are combined to form a sewage passing space, and electrodes are respectively arranged on the bottom surface of the sewage passing groove of each reactor inner core;
the reactor is characterized in that the reactor shell is provided with a reactor inner core accommodating groove, the reactor inner core is integrally inserted into the reactor inner core accommodating groove, the sewage passing space is located on the inner side of the reactor shell, the reactor shell is provided with an input connector and an output connector which are respectively communicated with the sewage passing space, the input connector is communicated with one end of a sewage conveying pipe, the other end of the sewage conveying pipe is communicated with the output end of a peristaltic pump, and the input end of the peristaltic pump is communicated with an external sewage source.
The electrode arranged on the bottom surface of the sewage passing groove of one reactor inner core is an anode electrode, and the electrode arranged on the bottom surface of the sewage passing groove of the other reactor inner core is a cathode electrode.
The two reactor cores are identical in structure and are symmetrically arranged in the reactor core accommodating grooves.
And electrode mounting grooves are formed in the bottom surface of the sewage passing groove of each reactor inner core.
And a gasket is arranged in the electrode mounting groove, and the electrode is fixed on the inner side of the gasket.
The bottom surface of each electrode mounting groove of the reactor inner core is provided with a conductor insertion groove, one side surface of each reactor inner core is provided with a conductor insertion opening, each conductor insertion opening of the reactor inner core is communicated with the electrode mounting groove of the reactor inner core, and an external conductor is inserted into the conductor insertion groove of the corresponding reactor inner core through the conductor insertion opening and is connected with an electrode in the reactor inner core for conduction.
The reactor inner core accommodating groove is formed in the top surface of the reactor shell, and each conductor inserting opening is formed in the corresponding top surface of the reactor inner core.
The input joint is communicated with the lower part of the sewage passing space, and the output joint is communicated with the upper part of the sewage passing space.
The input and output connectors are located on opposite sides of the reactor housing, respectively.
The utility model has the advantages and positive effects that:
according to the utility model, through the matched arrangement of the peristaltic pump, the sewage conveying pipe, the reactor shell and the two reactor cores provided with the electrodes, continuous flow can be used for replacing intermittent flow, pollutants can be directly removed from the continuous flow, water quality is optimized, the treated water quantity can be greatly increased, and the occupied area is saved; when different treatment requirements are met, the inner core of the reactor can be pulled out from the reactor shell, the corresponding electrode is replaced and then placed in the reactor shell again, and the reactor is convenient to use and high in applicability.
Drawings
FIG. 1 is a schematic diagram of the overall structure of the present utility model;
FIG. 2 is a schematic structural view of the reactor core of the present utility model;
FIG. 3 is a schematic view showing the internal structure of the reactor shell of the present utility model;
fig. 4 is a schematic view of an arrangement structure of an electrode according to the present utility model.
In the figure: the peristaltic pump 1, the sewage delivery pipe 2, the reactor shell 3, the reactor inner core 4, the sewage passing groove 41, the electrode mounting groove 42, the conductor inserting groove 43, the conductor inserting hole 44, the electrode 5, the input connector 6, the output connector 7 and the gasket 8.
Detailed Description
The utility model is described in further detail below with reference to fig. 1-4.
A continuous flow electrochemical reactor, as shown in FIGS. 1-4, comprises a peristaltic pump 1, a sewage delivery tube 2, a reactor shell 3 and two reactor cores 4.
A sewage passing groove 41 is formed in one side face of each reactor inner core 4, the two reactor inner cores 4 are mutually attached to form a reactor inner core whole, the sewage passing grooves 41 of the two reactor inner cores 4 are combined to form a sewage passing space, and electrodes 5 are respectively arranged on the bottom face of the sewage passing groove 41 of each reactor inner core 4.
The top surface of the reactor shell 3 is provided with a reactor inner core accommodating groove, the reactor inner core is integrally inserted into the reactor inner core accommodating groove, and the sewage is positioned at the inner side of the reactor shell 3 through the space. In the embodiment, the two reactor cores 4 have the same structure and are symmetrically arranged in the reactor core accommodating groove, so that the installation and the replacement are convenient. The reactor shell 3 is provided with an input connector 6 and an output connector 7 which are respectively communicated with sewage through a space, the input connector 6 is communicated with one end of the sewage conveying pipe 2, the other end of the sewage conveying pipe 2 is communicated with the output end of the peristaltic pump 1, and the input end of the peristaltic pump 1 is communicated with an external sewage source. In this embodiment, peristaltic pump 1 is a commercially available product and is controlled by an external controller. In this embodiment, the electrode 5 installed on the bottom surface of the sewage passing groove 41 of one reactor core 4 is an anode electrode, the electrode 5 installed on the bottom surface of the sewage passing groove 41 of the other reactor core 4 is a cathode electrode, and the electrode 5 can be an electrode member made of a corresponding material according to the prior art according to the treatment requirement. In this embodiment both reactor cores 4 are provided with circular electrodes 5.
Specifically, in this embodiment, the bottom surface of the sewage passing groove 41 of each reactor inner core 4 is provided with an electrode mounting groove 42, a circular gasket 8 is arranged in the electrode mounting groove 42, and the electrode 5 is fixed on the inner side of the gasket 8 through size fit, so that the electrode 5 is convenient to mount and fix. The gasket 8 in this embodiment is made of a waterproof material of the prior art. In this embodiment, the bottom surface of the electrode mounting groove 42 of each reactor core 4 is provided with a conductor insertion groove 43, the top surface of each reactor core 4 is provided with a conductor insertion groove 44, the conductor insertion groove 44 of each reactor core 4 is communicated with the electrode mounting groove 42 of the reactor core 4, and an external conductor can be conveniently inserted into the conductor insertion groove 43 of the corresponding reactor core 4 through the conductor insertion groove 44 and is electrically connected with the electrode 5 inside the reactor core 4, so that the disassembly is convenient. The reactor core accommodating groove is formed in the top surface of the reactor shell 3, and each conductor inserting opening 44 is formed in the top surface of the corresponding reactor core 4, so that the reactor core 4 can be conveniently taken and placed from the same side and the external conductors can be conveniently connected.
Specifically, in the present embodiment, the input joint 6 and the output joint 7 are respectively located on opposite side surfaces of the reactor housing 3, the input joint 6 communicates with a lower portion of the sewage passing space, and the output joint 7 communicates with an upper portion of the sewage passing space, so that sewage flowing through the sewage passing space is sufficiently treated.
Working principle:
when the peristaltic pump 1 is used, sewage of a communicated external sewage source is pumped into a sewage passing space inside the reactor shell 3 through the sewage conveying pipe 2 and the input joint 6, the electrodes 5 arranged in the two reactor inner cores 4 are connected with external conductors and electrified, so that the sewage flowing through the electrodes 5 in the sewage passing space is subjected to electrochemical oxidation reaction, thereby realizing continuous flow pollutant removal and water quality optimization, and the treated sewage flows out through the output joint 7; after the end of the reaction, the two reactor cores 4 can be pulled out of the reactor housing 3, or when different treatment requirements are met, the reactor cores 4 can be pulled out of the reactor housing 3, and the corresponding electrodes 5 can be replaced and then placed in the reactor housing 3 again.
Claims (9)
1. A continuous flow electrochemical reactor characterized by: comprises a peristaltic pump (1), a sewage conveying pipe (2), a reactor shell (3) and two reactor inner cores (4);
a sewage passing groove (41) is formed in one side surface of each reactor inner core (4), the two reactor inner cores (4) are mutually attached to form a reactor inner core whole, the sewage passing grooves (41) of the two reactor inner cores (4) are combined to form a sewage passing space, and electrodes (5) are respectively arranged on the bottom surface of the sewage passing groove (41) of each reactor inner core (4);
the reactor is characterized in that a reactor inner core accommodating groove is formed in the reactor outer shell (3), the reactor inner core is integrally inserted into the reactor inner core accommodating groove, sewage is located inside the reactor outer shell (3) through a space, an input connector (6) and an output connector (7) which are respectively communicated with the sewage through the space are arranged on the reactor outer shell (3), the input connector (6) is communicated with one end of the sewage conveying pipe (2), the other end of the sewage conveying pipe (2) is communicated with the output end of the peristaltic pump (1), and the input end of the peristaltic pump (1) is communicated with an external sewage source.
2. A continuous flow electrochemical reactor according to claim 1, characterized in that: the electrode (5) arranged on the bottom surface of the sewage passing groove (41) of one reactor inner core (4) is an anode electrode, and the electrode (5) arranged on the bottom surface of the sewage passing groove (41) of the other reactor inner core (4) is a cathode electrode.
3. A continuous flow electrochemical reactor according to claim 1, characterized in that: the two reactor cores (4) are identical in structure and are symmetrically arranged in the reactor core accommodating grooves.
4. A continuous flow electrochemical reactor according to claim 1, characterized in that: an electrode mounting groove (42) is formed in the bottom surface of the sewage passing groove (41) of each reactor inner core (4).
5. A continuous flow electrochemical reactor according to claim 4, characterized in that: a gasket (8) is arranged in the electrode mounting groove (42), and the electrode (5) is fixed on the inner side of the gasket (8).
6. A continuous flow electrochemical reactor according to claim 4, characterized in that: a conductor insertion groove (43) is formed in the bottom surface of each electrode installation groove (42) of each reactor inner core (4), a conductor insertion opening (44) is formed in one side surface of each reactor inner core (4), each conductor insertion opening (44) of each reactor inner core (4) is communicated with each electrode installation groove (42) of the corresponding reactor inner core (4), and an external conductor is inserted into the corresponding conductor insertion groove (43) of the corresponding reactor inner core (4) through the conductor insertion opening (44) and is connected with an electrode (5) inside the reactor inner core (4) to conduct electricity.
7. A continuous flow electrochemical reactor according to claim 6, characterized in that: the reactor inner core accommodating groove is formed in the top surface of the reactor shell (3), and each conductor inserting opening (44) is formed in the corresponding top surface of the reactor inner core (4).
8. A continuous flow electrochemical reactor according to claim 1, characterized in that: the input joint (6) is communicated with the lower part of the sewage passing space, and the output joint (7) is communicated with the upper part of the sewage passing space.
9. A continuous flow electrochemical reactor according to claim 1, characterized in that: the inlet connection (6) and the outlet connection (7) are each located on opposite sides of the reactor housing (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321957850.1U CN220467666U (en) | 2023-07-25 | 2023-07-25 | Continuous flow electrochemical reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321957850.1U CN220467666U (en) | 2023-07-25 | 2023-07-25 | Continuous flow electrochemical reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220467666U true CN220467666U (en) | 2024-02-09 |
Family
ID=89804043
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321957850.1U Active CN220467666U (en) | 2023-07-25 | 2023-07-25 | Continuous flow electrochemical reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220467666U (en) |
-
2023
- 2023-07-25 CN CN202321957850.1U patent/CN220467666U/en active Active
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