CN218026372U

CN218026372U - Electrolytic separation tank with barrel type structure

Info

Publication number: CN218026372U
Application number: CN202221198392.3U
Authority: CN
Inventors: 陈鹏; 陈俊毅
Original assignee: Shanghai Rui Analysis Scientific Instrument Co ltd
Current assignee: Shanghai Rui Analysis Scientific Instrument Co ltd
Priority date: 2022-05-10
Filing date: 2022-05-10
Publication date: 2022-12-13
Anticipated expiration: 2032-05-10

Abstract

The utility model discloses a generator technical field's electrolytic separation pond of bucket formula structure, including bucket formula electrolytic bath, the inside of bucket formula electrolytic bath is run through and is installed the inlet tube, the top run through connection of bucket formula electrolytic bath has the blast pipe, and the one end of blast pipe is connected with the vapor pump, and the one end of vapor pump is connected with the vortex drying tube, and the surface threaded connection of vortex drying tube has dry box, and the one end veneer of vortex drying tube is connected with exhaust passage. The utility model discloses a setting and the scroll drying tube of bucket formula electrolytic bath coaxial axis can prolong the dry route that contains vapor gas when saving equipment space, and every dry box can carry out at least time reciprocal drying to containing vapor gas, has promoted the drying effect that contains vapor gas greatly.

Description

Electrolytic separation tank with barrel type structure

Technical Field

The utility model relates to the technical field of generators, in particular to an electrolytic separation tank with a barrel structure.

Background

The hydrogen generator is a self-regulating hydrogen generator for a hydrogen fuel cell. When the hydrogen generator is used in an electrolytic separation tank, the gas pressure in the generator is required to be adjusted so as to avoid the influence of the excessive gas pressure in the tank on the reaction process of the electrolytic separation tank of the hydrogen generator. Based on this, the utility model designs an electrolytic separation pond of bucket formula structure to solve above-mentioned problem.

SUMMERY OF THE UTILITY MODEL

An object of the utility model is to provide an electrolytic separation pond of bucket formula structure to solve the problem that proposes among the above-mentioned background art.

In order to achieve the above purpose, the utility model provides a following technical scheme: the utility model provides an electrolytic separation pond of bucket formula structure, includes bucket formula electrolytic bath, and the inside of bucket formula electrolytic bath is run through and is installed the inlet tube, the top through connection of bucket formula electrolytic bath has the blast pipe, and the one end of blast pipe is connected with the vapor pump, and the one end of vapor pump is connected with the vortex drying tube, and the surperficial threaded connection of vortex drying tube has dry box, and the one end veneer of vortex drying tube is connected with exhaust passage.

Preferably, the bottom of the barrel-type electrolytic cell is clamped with symmetrical support frames.

Preferably, the input end of the steam pump is electrically connected with an external power supply.

Preferably, the exhaust pipe is an L-shaped hollow PC pipe.

Preferably, the vortex drying tube is in a hollow vortex line, and the central point of the vortex drying tube is superposed with the central point of the cross section of the barrel-type electrolytic cell.

Preferably, the drying box is provided with threely, three the drying box is equidistant arranges in proper order, and the top and the bottom of drying box are fixedly connected with screwed joint respectively, and screwed joint is provided with a plurality of.

Preferably, the inner wall of drying box is fixed with the spacing frame of frame, and the joint has the drying plate between two adjacent spacing frames of frame.

Preferably, one end of the water inlet pipe is fixedly connected with a hexagonal joint.

Compared with the prior art, the beneficial effects of the utility model are that:

(1) The utility model has the advantages that the drying path of the gas containing water vapor can be prolonged while the equipment space is saved by arranging the vortex-shaped drying tube which is coaxial with the barrel-type electrolytic cell, each drying box can carry out at least one-time reciprocating drying on the gas containing water vapor, the drying effect of the gas containing water vapor is greatly improved, and the dried gas can be discharged through the exhaust passage 2;

(2) The utility model discloses a set up the overall arrangement structure of the central point coincidence of vortex drying tube and bucket formula electrolytic bath cross section, be favorable to rationalizing the installation space of vortex drying tube to reduce the volume that occupies of equipment, screwed joint is used for connecting the vortex drying tube, and the spacing frame of frame is used for spacing and holds in the palm the drying plate.

Drawings

In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings used in the description of the embodiments will be briefly introduced below, and it is obvious that the drawings in the following description are only some embodiments of the present invention, and it is obvious for those skilled in the art that other drawings can be obtained according to these drawings without creative efforts.

FIG. 1 is a three-dimensional structure diagram of the electrolytic separation cell of the barrel structure of the utility model;

FIG. 2 is an enlarged view of A in FIG. 1 of the electrolytic separation cell of the barrel structure of the present invention;

FIG. 3 is a front view of the electrolytic separation cell of the bucket structure of the present invention;

FIG. 4 is a structural view of the interior of the drying box of the electrolytic separation cell of the barrel structure of the present invention.

In the drawings, the components represented by the respective reference numerals are listed below:

1. a support frame; 2. an exhaust passage; 3. a swirl drying tube; 4. drying the box; 5. a threaded joint; 6. a frame type limiting frame; 7. drying the plate; 8. a water vapor pump; 9. an exhaust pipe; 10. a barrel-type electrolytic cell; 11. a water inlet pipe; 12. a hexagonal joint.

Detailed Description

The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by a person skilled in the art without making creative efforts belong to the protection scope of the present invention.

Referring to fig. 1-4, the present invention provides a technical solution: an electrolytic separation tank with a barrel-type structure comprises a barrel-type electrolytic tank 10, wherein symmetrical support frames 1 are clamped at the bottom of the barrel-type electrolytic tank 10, a water inlet pipe 11 penetrates through the interior of the barrel-type electrolytic tank 10, a hexagonal joint 12 is fixedly connected to one end of the water inlet pipe 11, an exhaust pipe 9 penetrates through the top of the barrel-type electrolytic tank 10, one end of the exhaust pipe 9 is connected with a steam pump 8, one end of the steam pump 8 is connected with a vortex-shaped drying pipe 3, the surface of the vortex-shaped drying pipe 3 is in threaded connection with three drying boxes 4, the three drying boxes 4 are arranged in sequence at equal intervals, and one end of the vortex-shaped drying pipe 3 is connected with an exhaust passage 2 in a gluing mode;

wherein, the installation of the gaseous drying tube of reasonable overall arrangement vortex of bucket formula electrolytic bath 10 is convenient for, thereby promote the dry effect of steam when saving space, during the use, let in the interior pure water of bucket formula electrolytic bath 10 through inlet tube 11, the electrolysis aquatic products produces hydrogen and oxygen, through starting vapor pump 8, the gas that contains steam passes through blast pipe 9 and gets into in vapor pump 8, send into the gaseous moisture of moisture into vortex drying tube 3 by vapor pump 8 in, carry out many times drying by three drying box 4, get rid of the moisture in the gas, can discharge dry gas through exhaust passage 2, the device is through setting up the gaseous drying tube of vortex 3 with the axle center with bucket formula electrolytic bath 10, can prolong the gaseous dry route that contains steam when saving equipment space, every drying box 4 can carry out at least 4 reciprocal drying to the gas that contains steam, the gaseous dry effect that contains steam has been promoted greatly.

Referring to fig. 1-4, an input end of a vapor pump 8 is electrically connected with an external power supply, an exhaust pipe 9 is an L-shaped hollow PC pipe, a vortex drying pipe 3 is in a hollow vortex line direction, a center point of the vortex drying pipe 3 is coincident with a center point of a cross section of a barrel type electrolytic cell 10, the top and the bottom of a drying box 4 are respectively and fixedly connected with a plurality of threaded joints 5, frame type limiting frames 6 are fixed on the inner wall of the drying box 4, and a drying plate 7 is clamped between two adjacent frame type limiting frames 6;

wherein, connect hollow blast pipe 9 through the top at bucket formula electrolytic bath 10, can in time discharge the gas of top gathering in bucket formula electrolytic bath 10, through the overall arrangement structure who sets up the coincidence of central point of vortex drying tube 3 and bucket formula electrolytic bath 10 cross section, be favorable to rationalizing the installation space of vortex drying tube 3 to reduce the volume that occupies of equipment, screwed joint 5 is used for connecting vortex drying tube 3, frame spacing 6 is used for spacing and holds dry plate 7.

Holistic theory of operation does, during the use, lets in pure water in the bucket formula electrolytic bath 10 through inlet tube 11, and the electrolysis aquatic products produces hydrogen and oxygen, through starting vapor pump 8, and in the gas that contains steam passed through blast pipe 9 and got into vapor pump 8, sent into the vortex drying tube 3 with the gas that contains steam by vapor pump 8 in, carried out many times by three drying box 4 and dried, got rid of the moisture in the gas, can discharge dry gas through exhaust passage 2.

In the description herein, references to the description of "one embodiment," "an example," "a specific example," etc., mean that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the invention. In this specification, the schematic representations of the terms used above do not necessarily refer to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples.

The preferred embodiments of the present invention disclosed above are intended only to help illustrate the present invention. The preferred embodiments are not intended to be exhaustive or to limit the invention to the precise embodiments disclosed. Obviously, many modifications and variations are possible in light of the above teaching. The embodiments were chosen and described in order to best explain the principles of the invention and its practical applications, thereby enabling others skilled in the art to best understand the invention and its practical application. The present invention is limited only by the claims and their full scope and equivalents.

Claims

1. The utility model provides an electrolytic separation pond of bucket formula structure, includes bucket formula electrolytic bath (10), and the inside of bucket formula electrolytic bath (10) is run through and is installed inlet tube (11), its characterized in that: the top through connection of bucket formula electrolytic bath (10) has blast pipe (9), and the one end of blast pipe (9) is connected with vapor pump (8), and the one end of vapor pump (8) is connected with vortex drying tube (3), and the surface threaded connection of vortex drying tube (3) has drying box (4), and the one end veneer of vortex drying tube (3) is connected with exhaust passage (2).

2. The electrolytic separation cell of a bucket structure of claim 1, wherein: the bottom of the barrel-type electrolytic cell (10) is clamped with symmetrical support frames (1).

3. The electrolytic separation cell of a bucket structure of claim 1, wherein: the input end of the steam pump (8) is electrically connected with an external power supply.

4. The electrolytic separation cell of a bucket structure of claim 1, wherein: the exhaust pipe (9) is an L-shaped hollow PC pipe.

5. The electrolytic separation cell of a bucket structure of claim 1, wherein: the vortex drying tube (3) is in a hollow vortex line trend, and the central point of the vortex drying tube (3) is superposed with the central point of the cross section of the barrel type electrolytic cell (10).

6. The electrolytic separation cell of a bucket structure of claim 1, wherein: drying box (4) are provided with threely, three drying box (4) are equidistant arranges in proper order, and the top and the bottom of drying box (4) are fixedly connected with screwed joint (5) respectively, and screwed joint (5) are provided with a plurality of.

7. The electrolytic separation cell of a bucket structure according to claim 6, wherein: the inner wall of the drying box (4) is fixed with frame-type limiting frames (6), and a drying plate (7) is clamped between two adjacent frame-type limiting frames (6).

8. The electrolytic separation cell of a bucket structure of claim 1, wherein: one end of the water inlet pipe (11) is fixedly connected with a hexagonal joint (12).