CN220918675U - Water electrolysis hydrogen production purification jar - Google Patents
Water electrolysis hydrogen production purification jar Download PDFInfo
- Publication number
- CN220918675U CN220918675U CN202322743686.0U CN202322743686U CN220918675U CN 220918675 U CN220918675 U CN 220918675U CN 202322743686 U CN202322743686 U CN 202322743686U CN 220918675 U CN220918675 U CN 220918675U
- Authority
- CN
- China
- Prior art keywords
- drying tower
- fixedly connected
- tube
- pipe
- deoxidizing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 239000001257 hydrogen Substances 0.000 title claims abstract description 25
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 25
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 24
- 238000000746 purification Methods 0.000 title claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 18
- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 17
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 16
- 238000001035 drying Methods 0.000 claims abstract description 164
- 238000010438 heat treatment Methods 0.000 claims abstract description 56
- 230000002093 peripheral effect Effects 0.000 claims abstract description 18
- 230000000149 penetrating effect Effects 0.000 claims abstract description 14
- 238000009413 insulation Methods 0.000 claims abstract description 12
- 238000007599 discharging Methods 0.000 claims abstract description 10
- 210000001503 joint Anatomy 0.000 claims description 24
- 239000000126 substance Substances 0.000 abstract description 2
- 238000009434 installation Methods 0.000 description 13
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 238000010586 diagram Methods 0.000 description 5
- 239000007789 gas Substances 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000003054 catalyst Substances 0.000 description 3
- 238000001514 detection method Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 230000007306 turnover Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000002274 desiccant Substances 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 239000002808 molecular sieve Substances 0.000 description 2
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000033116 oxidation-reduction process Effects 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Landscapes
- Drying Of Gases (AREA)
Abstract
The utility model discloses a purification cylinder for hydrogen production by water electrolysis, which relates to the technical field of chemical equipment and comprises a drying tower and a deoxidizing tank, wherein the drying tower and the deoxidizing tank are connected through a pipeline, the drying tower comprises a drying tower supporting column, the upper surface of the drying tower supporting column is fixedly connected with a drying tower lower end socket, the cross section of the drying tower lower end socket is a semicircular arc, the upper surface of the drying tower lower end socket is fixedly connected with a drying tower outer pipe, the upper surface of the drying tower outer pipe is fixedly connected with a drying tower upper end socket, the top wall of the drying tower upper end socket is fixedly connected with a first heating rod peripheral pipe in a penetrating manner, and the side wall of the drying tower lower end socket is fixedly connected with a drying tower discharging pipe in a penetrating manner. According to the utility model, the heat insulation layer is arranged, the heating wire is wound between the heat insulation layer and the outer tube of the drying tower, the heat is uniformly heated when the drying tower is heated through the heat insulation layer and the heating wire, the temperature difference is reduced, and the temperature parameter is measured and controlled through the temperature transmitter.
Description
Technical Field
The utility model relates to the technical field of chemical equipment, in particular to a purification cylinder for water electrolysis hydrogen production.
Background
The hydrogen contains a large amount of impurities, a small amount of chlorine, a small amount of nitrogen, carbon dioxide and the like, wherein in order to purify the hydrogen, the oxygen in the hydrogen needs to be separated and removed, and a palladium catalyst on an alumina carrier is needed to convert the oxygen in the oxygen into water vapor through catalytic oxidation reduction. The existing drying tower for water electrolysis hydrogen production purification has large upper and lower temperature difference, the temperature is Yu Wenda, the control cannot be carried out, and the heating cylinder molecular sieve is heated unevenly.
Based on the above, the water electrolysis hydrogen production purification cylinder can eliminate the defects of the prior device.
Disclosure of utility model
The utility model aims to provide a water electrolysis hydrogen production purification cylinder, which solves the problems that the temperature difference between the upper part and the lower part of a drying tower in the background technology is large, the temperature is Yu Wenda, the molecular sieve of a heating cylinder cannot be controlled, and the heating is not uniform.
In order to achieve the above purpose, the present utility model provides the following technical solutions:
The utility model provides a water electrolysis hydrogen manufacturing purification jar, includes drying tower and deoxidization jar, pass through pipe connection between drying tower and the deoxidization jar, the drying tower includes the drying tower support column, fixed surface is connected with the drying tower lower cover on the drying tower support column, the drying tower lower cover cross-section is the semicircle, fixed surface is connected with the drying tower outer tube on the drying tower lower cover, fixed surface is connected with the drying tower upper cover on the drying tower outer tube, drying tower upper cover roof runs through the first heating rod peripheral pipe of fixedly connected with, drying tower lower cover lateral wall runs through fixedly connected with drying tower discharging pipe, drying tower upper cover lateral wall runs through fixedly connected with drying tower inlet pipe, the lateral wall that first heating rod peripheral pipe is located the drying tower outer tube runs through fixedly connected with drying tower air inlet, drying tower support column, drying tower discharging pipe, drying air outlet, drying tower inlet all are provided with the flange, drying tower air inlet is kept away from the one end of drying tower outer tube.
Based on the technical scheme, the utility model also provides the following optional technical schemes:
in one alternative: the deoxidization jar includes the deoxidization jar support column, deoxidization jar support column upper surface fixedly connected with deoxidization jar lower head, deoxidization jar lower head upper surface fixedly connected with deoxidization jar outer tube, deoxidization jar outer tube upper surface fixedly connected with deoxidization jar upper head, deoxidization jar upper head roof runs through fixedly connected with second and places the pipe, deoxidization jar outer tube lateral wall runs through fixedly connected with deoxidization jar air inlet, deoxidization jar gas outlet, business turn over material pipe, deoxidization jar gas outlet and business turn over material pipe are located same with the horizontal plane, deoxidization jar air inlet is located deoxidization jar gas outlet top, deoxidization jar air inlet, deoxidization jar support column, deoxidization jar gas outlet, business turn over material pipe keep away from deoxidization jar outer tube's one end all is provided with the flange.
In one alternative: the utility model discloses a drying tower, including drying tower outer tube, first temperature transmitter pipe of drying tower outer tube lateral wall, second temperature transmitter pipe, first installation piece of drying tower outer tube lateral wall fixedly connected with and second installation piece, the one end that the second temperature transmitter pipe is located the drying tower outer tube runs through fixedly connected with first installation piece, the one end that first temperature transmitter pipe is located the drying tower outer tube runs through fixedly connected with second installation piece, first installation piece and second installation piece inside wall all are provided with the screw thread, first installation piece threaded connection has the second temperature transmitter, second installation piece threaded connection has first temperature transmitter.
In one alternative: the utility model discloses a drying tower butt joint pipe, including first heating rod peripheral pipe inside wall sliding connection, first placing pipe runs through and extends to outside the drying tower outer tube, the first one end that places the pipe and be located outside the drying tower outer tube is provided with the flange, first heating rod peripheral pipe top is provided with the flange, first heating rod peripheral pipe passes through flange joint with first placing pipe, the flange upper surface of first placing pipe is provided with the drying tower and connects the pipe, drying tower connects the pipe upper surface fixedly connected with drying tower fast-assembling chuck, first placing pipe inside wall has placed first heating rod, first heating rod runs through and extends to in the drying tower connects the pipe, the hole has been seted up to drying tower butt joint pipe lateral wall, the heating rod detection line of first heating rod runs through the hole and extends to outside the drying tower butt joint pipe.
In one alternative: the outer side wall of the outer tube of the drying tower is fixedly connected with an insulating layer, and a heating wire is wound between the insulating layer and the outer tube of the drying tower.
In one alternative: the inner side wall of the peripheral tube of the first heating rod is provided with three temperature sensors.
In one alternative: the second placing pipe inner side wall penetrates through the second heating rod in a sliding mode, the upper surface of the second mounting block is fixedly connected with a deoxidizing tank butt joint pipe, the upper surface of the deoxidizing tank butt joint pipe is fixedly connected with a deoxidizing tank fast-assembly chuck, and the second heating rod penetrates through and extends into the deoxidizing tank butt joint pipe.
In one alternative: the deoxidization jar outer tube lateral wall runs through fixedly connected with third temperature transmitter pipe, deoxidization jar outer tube lateral wall fixedly connected with third installation piece, third temperature transmitter pipe runs through and extends to in the third installation piece with third installation piece inside wall fixed connection, third installation piece inside wall is provided with the screw thread, third installation piece threaded connection has third temperature transmitter.
Compared with the prior art, the utility model has the following beneficial effects:
According to the utility model, the heat insulation layer is arranged, the heating wire is wound between the heat insulation layer and the outer tube of the drying tower, so that the heating of the drying tower can be uniform when the drying tower is heated, the temperature difference is reduced, and the temperature parameter is measured and controlled through the temperature transmitter.
Drawings
Fig. 1 is a schematic diagram of a drying tower according to the present utility model.
Fig. 2 is a schematic diagram of the bottom of the drying tower of the present utility model.
Fig. 3 is a schematic top view of a drying tower according to the present utility model.
Fig. 4 is a top view showing the internal structure of the drying tower of the present utility model.
Fig. 5 is an enlarged view of fig. 3 a in accordance with the present utility model.
Fig. 6 is an enlarged view of fig. 4 at B in accordance with the present utility model.
Fig. 7 is a schematic diagram of the top insulation layer structure of the drying tower according to the present utility model.
Fig. 8 is a schematic diagram of a mechanism of a bottom insulation layer of a drying tower according to the present utility model.
Fig. 9 is a schematic view of a heating rod according to the present utility model.
FIG. 10 is a schematic view of the structure of the deoxidizing pot of the present utility model.
FIG. 11 is a schematic diagram of the top structure of the deoxidizing pot of the present utility model.
FIG. 12 is a schematic view of the bottom structure of the deoxidizing pot of the present utility model.
FIG. 13 is a schematic top view of the deoxidizer of the present utility model.
Fig. 14 is an enlarged view of fig. 12 at C in accordance with the present utility model.
Reference numerals annotate: a drying tower support column, a first temperature transmitter, a 3 drying tower discharge pipe, a 4 drying tower lower head, a 5 first temperature transmitter pipe, a 6 first placing pipe, a 7 drying tower outer pipe, a 8 first heating rod, a 9 first heating rod peripheral pipe, a 10 drying tower air outlet, a 11 drying tower feed pipe, a 12 drying tower fast-assembling chuck, a 13 drying tower butt joint pipe, a 14 heating rod detection line, a 15 drying tower air inlet, a 16 second temperature transmitter, a 17 drying tower upper head, a 18 second temperature transmitter pipe, a 19 first mounting block, a 20 second mounting block, a 21 insulation layer, a 22 heating wire, a 23 temperature sensor, a 24 deoxidizing tank outer pipe, a 25 deoxidizing tank air inlet, a 26 second placing pipe, a 27 second heating rod, a 28 deoxidizing tank butt joint pipe, a 29 deoxidizing tank fast-assembling chuck, a 30 deoxidizing tank upper head, a 31 deoxidizing tank lower head, a 32 third temperature transmitter, a 33 third temperature transmitter pipe, a 34 third mounting block, a 35 deoxidizing tank support column, a 36 deoxidizing tank air outlet and air inlet, a 37 feeding pipe, a 101 drying tower, and 102 deoxidizing tank.
Detailed Description
The present utility model will be described in further detail with reference to the drawings and examples, in order to make the objects, technical solutions and advantages of the present utility model more apparent.
In one embodiment, as shown in fig. 1-14, a purification jar for producing hydrogen by water electrolysis comprises a drying tower 101 and a deoxidizing tank 102, wherein the drying tower 101 and the deoxidizing tank 102 are connected through a pipeline, the drying tower 101 comprises a drying tower supporting column 1, a drying tower lower end enclosure 4 is fixedly connected to the upper surface of the drying tower supporting column 1, the cross section of the drying tower lower end enclosure 4 is a semicircular arc, a drying tower outer tube 7 is fixedly connected to the upper surface of the drying tower lower end enclosure 4, a drying tower upper end enclosure 17 is fixedly connected to the upper wall of the drying tower outer tube 7, a first heating rod peripheral tube 9 is fixedly connected to the top wall of the drying tower upper end enclosure 17, a drying tower feeding tube 3 is fixedly connected to the side wall of the drying tower lower end enclosure 4, a drying tower air inlet 15 is fixedly connected to the side wall of the drying tower outer tube 7, and flanges are arranged at one ends of the drying tower supporting column 1, the drying tower feeding tube 3, the drying tower air outlet 10, the drying tower feeding tube 11 and the drying tower air inlet 15 far away from the drying tower outer tube 7.
In one embodiment, as shown in fig. 11 and 12, the deoxidizing pot 102 includes a deoxidizing pot support post 35, the deoxidizing pot support post 35 is fixedly connected with a deoxidizing pot lower end socket 31 on the upper surface, the deoxidizing pot outer tube 24 is fixedly connected with a deoxidizing pot upper end socket 30 on the upper surface of the deoxidizing pot lower end socket 31, the top wall of the deoxidizing pot upper end socket 30 is fixedly connected with a second placing tube 26, the side wall of the deoxidizing pot outer tube 24 is fixedly connected with a deoxidizing pot air inlet 25, a deoxidizing pot air outlet 36 and a feeding and discharging tube 37, the deoxidizing pot air outlet 36 and the feeding and discharging tube 37 are located on the same horizontal plane, the deoxidizing pot air inlet 25 is located above the deoxidizing pot air outlet 36, and flanges are arranged at one ends of the deoxidizing pot air inlet 25, the deoxidizing pot support post 35, the deoxidizing pot air outlet 36 and the feeding and discharging tube 37 away from the deoxidizing pot outer tube 24. The hydrogen gas containing oxygen is introduced into the deoxidizer outer tube 24 from the deoxidizer gas inlet 25, and then the deoxidizer catalyst is introduced into the deoxidizer outer tube 24 from the feed-in/discharge tube 37.
In one embodiment, as shown in fig. 2 and 3, the side wall of the outer tube 7 of the drying tower is fixedly connected with a first temperature transmitter tube 5 and a second temperature transmitter tube 18 in a penetrating manner, the second temperature transmitter tube 18 is located above the first temperature transmitter tube 5, the outer side wall of the outer tube 7 of the drying tower is fixedly connected with a first mounting block 19 and a second mounting block 20, one end of the second temperature transmitter tube 18 located outside the outer tube 7 of the drying tower is fixedly connected with the first mounting block 19 in a penetrating manner, one end of the first temperature transmitter tube 5 located outside the outer tube 7 of the drying tower is fixedly connected with the second mounting block 20 in a penetrating manner, the inner side walls of the first mounting block 19 and the second mounting block 20 are respectively provided with threads, the first mounting block 19 is in threaded connection with the second temperature transmitter 16, and the second mounting block 20 is in threaded connection with the first temperature transmitter 2. Is transported into the outer drying tower tube 7 through the air inlet 15 of the drying tower, and the drying agent is added into the outer drying tower tube 7 from the feeding pipe 11 of the drying tower.
In one embodiment, as shown in fig. 2, the inner side wall of the peripheral tube 9 of the first heating rod is slidably connected with a first placing tube 6, the first placing tube 6 extends out of the outer tube 7 of the drying tower in a penetrating manner, one end of the first placing tube 6 located out of the outer tube 7 of the drying tower is provided with a flange, the top of the peripheral tube 9 of the first heating rod is provided with a flange, the peripheral tube 9 of the first heating rod is connected with the first placing tube 6 through the flange, the upper surface of the flange of the first placing tube 6 is provided with a drying tower butt joint tube 13, the upper surface of the drying tower butt joint tube 13 is fixedly connected with a drying tower quick-mounting chuck 12, the inner side wall of the first placing tube 6 is provided with a first heating rod 8, the first heating rod 8 extends into the inside of the butt joint tube 13 of the drying tower, the side wall of the butt joint tube 13 is provided with a hole, and a heating rod detection line 14 of the first heating rod 8 extends out of the butt joint tube 13 of the drying tower through the hole. The first heating rod 8 accelerates the drying rate.
In one embodiment, as shown in fig. 7 and 8, an insulation layer 21 is fixedly connected to the outer side wall of the outer tube 7 of the drying tower, and a heating wire 22 is wound between the insulation layer 21 and the outer tube 7 of the drying tower. The heat preservation layer 21 and the heating wire 22 can be heated uniformly when heating the drying tower, and the temperature difference is small.
In one embodiment, as shown in fig. 7 and 8, the first heater rod outer tube 9 is provided with three temperature sensors 23 on the inner side wall. And the temperature is detected at three positions, so that the method is safe and reliable.
In one embodiment, as shown in fig. 11 and 12, the inner side wall of the second placing pipe 26 is connected with a second heating rod 27 in a penetrating and sliding manner, the upper surface of the second mounting block 20 is fixedly connected with a deoxidizing tank butt joint pipe 28, the upper surface of the deoxidizing tank butt joint pipe 28 is fixedly connected with a deoxidizing tank quick-mounting chuck 29, and the second heating rod 27 extends into the deoxidizing tank butt joint pipe 28 in a penetrating manner. The rate of the deoxidation reaction is accelerated by the heating of the second placement tube 26.
In one embodiment, as shown in fig. 11 and 12, the side wall of the deoxidizing tank outer tube 24 is fixedly connected with a third temperature transmitter tube 33, the outer side wall of the deoxidizing tank outer tube 24 is fixedly connected with a third mounting block 34, the third temperature transmitter tube 33 extends into the third mounting block 34 and is fixedly connected with the inner side wall of the third mounting block 34, the inner side wall of the third mounting block 34 is provided with threads, and the third mounting block 34 is in threaded connection with a third temperature transmitter 32. Temperature transmitters are meters that convert a temperature variable into a transmissible standardized output signal for measurement and control of an industrial process temperature parameter.
The above embodiment discloses a purification cylinder for producing hydrogen by water electrolysis, firstly, hydrogen containing oxygen is introduced into an outer deoxidizing tube 24 from an air inlet 25 of a deoxidizing pot, then a deoxidizing catalyst is added into the outer deoxidizing pot 24 from an air inlet and outlet tube 37, the deoxidizing reaction rate is accelerated by heating of a second placing tube 26, the deoxidized hydrogen is discharged from an air outlet 36 of the deoxidizing pot, transported into an outer drying tube 7 through an air inlet 15 of a drying tower, a drying agent is added into the outer drying tube 7 from an air inlet 11 of the drying tower, and the dried hydrogen is discharged from an air outlet 10 of the drying tower after the drying rate is accelerated by a first heating rod 8, so that the deoxidizing and drying of the hydrogen are completed.
The foregoing is merely specific embodiments of the disclosure, but the protection scope of the disclosure is not limited thereto, and any person skilled in the art can easily think about changes or substitutions within the technical scope of the disclosure, and it is intended to cover the scope of the disclosure. Therefore, the protection scope of the present disclosure shall be subject to the protection scope of the claims.
Claims (8)
1. The utility model provides a water electrolysis hydrogen manufacturing purification jar, includes drying tower (101) and deoxidization jar (102), pass through pipe connection between drying tower (101) and deoxidization jar (102), a serial communication port, drying tower (101) are including drying tower support column (1), drying tower support column (1) upper surface fixedly connected with drying tower lower cover (4), drying tower lower cover (4) cross-section is the semicircle, drying tower lower cover (4) upper surface fixedly connected with drying tower outer tube (7), drying tower outer tube (7) upper surface fixedly connected with drying tower upper cover (17), drying tower upper cover (17) roof runs through fixedly connected with first heating rod peripheral pipe (9), drying tower lower cover (4) lateral wall runs through fixedly connected with drying tower discharging pipe (3), drying tower upper cover (17) lateral wall runs through fixedly connected with drying tower inlet pipe (11), lateral wall that first heating rod peripheral pipe (9) are located drying tower outer tube (7) runs through fixedly connected with drying tower (15), drying tower (1), drying tower outer tube (3), drying tower outer tube (10) and drying tower outer tube (15) are kept away from all to set up drying tower flange (15).
2. The water electrolysis hydrogen production purification cylinder according to claim 1, wherein the deoxidizing tank (102) comprises a deoxidizing tank supporting column (35), a deoxidizing tank lower end socket (31) is fixedly connected to the upper surface of the deoxidizing tank supporting column (35), a deoxidizing tank outer tube (24) is fixedly connected to the upper surface of the deoxidizing tank lower end socket (31), a deoxidizing tank upper end socket (30) is fixedly connected to the upper surface of the deoxidizing tank outer tube (24), a second placing tube (26) is fixedly connected to the top wall of the deoxidizing tank upper end socket (30) in a penetrating manner, a deoxidizing tank air inlet (25), a deoxidizing tank air outlet (36) and a feeding and discharging tube (37) are fixedly connected to the side wall of the deoxidizing tank outer tube (24), the deoxidizing tank air outlet (36) and the feeding and discharging tube (37) are located on the same horizontal plane, the deoxidizing tank air inlet (25) is located above the deoxidizing tank air outlet (36), and flanges are arranged at one ends of the deoxidizing tank air inlet (25), the deoxidizing tank supporting column (35), the deoxidizing tank air outlet (36) and the feeding and discharging tube (37) away from the deoxidizing tank outer tube (24).
3. The water electrolysis hydrogen production purification cylinder according to claim 2, wherein the side wall of the outer drying tower tube (7) is fixedly connected with a first temperature transmitter tube (5) and a second temperature transmitter tube (18) in a penetrating manner, the second temperature transmitter tube (18) is located above the first temperature transmitter tube (5), the outer side wall of the outer drying tower tube (7) is fixedly connected with a first mounting block (19) and a second mounting block (20), one end of the second temperature transmitter tube (18) located outside the outer drying tower tube (7) is fixedly connected with the first mounting block (19) in a penetrating manner, one end of the first temperature transmitter tube (5) located outside the outer drying tower tube (7) is fixedly connected with the second mounting block (20) in a penetrating manner, the inner side walls of the first mounting block (19) and the second mounting block (20) are provided with threads, the first mounting block (19) is fixedly connected with the second temperature transmitter (16) in a threaded manner, and the second mounting block (20) is in a threaded manner.
4. The water electrolysis hydrogen production purification jar according to claim 3, characterized in that, first heating rod peripheral tube (9) inside wall sliding connection has first tub (6) of placing, first tub (6) of placing runs through and extends to outside drying tower outer tube (7), first tub (6) of placing is provided with the flange in the one end that is located outside drying tower outer tube (7), first heating rod peripheral tube (9) top is provided with the flange, first heating rod peripheral tube (9) and first tub (6) of placing pass through flange joint, the flange upper surface of first tub (6) of placing is provided with drying tower butt joint pipe (13), drying tower butt joint pipe (13) upper surface fixed connection has drying tower fast-assembling chuck (12), first heating rod (8) have been placed to first tub (6) inside wall, first heating rod (8) run through and extend to in drying tower butt joint pipe (13), the hole has been seted up to drying tower butt joint pipe (13) lateral wall, heating wire (14) are passed through and are extended to outside drying tower butt joint pipe (13).
5. The purification cylinder for water electrolysis hydrogen production according to claim 1, wherein an insulation layer (21) is fixedly connected to the outer side wall of the outer tube (7) of the drying tower, and a heating wire (22) is wound between the insulation layer (21) and the outer tube (7) of the drying tower.
6. A hydrogen purification cylinder according to claim 1, characterized in that the inner side wall of the first heating rod peripheral tube (9) is provided with three temperature sensors (23).
7. A water electrolysis hydrogen production purification jar according to claim 3, wherein the second placing pipe (26) is provided with a second heating rod (27) penetrating through the inner side wall, the upper surface of the second mounting block (20) is fixedly connected with a deoxidizing tank butt joint pipe (28), the upper surface of the deoxidizing tank butt joint pipe (28) is fixedly connected with a deoxidizing tank fast-assembling chuck (29), and the second heating rod (27) penetrates through and extends into the deoxidizing tank butt joint pipe (28).
8. The purification cylinder for hydrogen production by water electrolysis according to claim 2, wherein a third temperature transmitter pipe (33) is fixedly connected to the side wall of the deoxidization tank outer pipe (24), a third mounting block (34) is fixedly connected to the outer side wall of the deoxidization tank outer pipe (24), the third temperature transmitter pipe (33) extends into the third mounting block (34) in a penetrating manner and is fixedly connected with the inner side wall of the third mounting block (34), threads are arranged on the inner side wall of the third mounting block (34), and a third temperature transmitter (32) is connected to the inner side wall of the third mounting block (34) in a threaded manner.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322743686.0U CN220918675U (en) | 2023-10-13 | 2023-10-13 | Water electrolysis hydrogen production purification jar |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322743686.0U CN220918675U (en) | 2023-10-13 | 2023-10-13 | Water electrolysis hydrogen production purification jar |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220918675U true CN220918675U (en) | 2024-05-10 |
Family
ID=90967430
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322743686.0U Active CN220918675U (en) | 2023-10-13 | 2023-10-13 | Water electrolysis hydrogen production purification jar |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220918675U (en) |
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2023
- 2023-10-13 CN CN202322743686.0U patent/CN220918675U/en active Active
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