PIPE-TYPE ELECTROLYSIS CELL
20170283962 · 2017-10-05
Assignee
Inventors
- Boong Ik Jung (Cheongju, KR)
- Jung Sik Kim (Cheongju, KR)
- Hyun Su SHIN (Daejeon, KR)
- Min Yong Kim (Cheongju, KR)
Cpc classification
C25B1/34
CHEMISTRY; METALLURGY
C25B9/63
CHEMISTRY; METALLURGY
International classification
C25B1/34
CHEMISTRY; METALLURGY
Abstract
Disclosed is a pipe-type electrolysis cell including: a pair of terminal electrodes including an outer electrode and an inner electrode that are electrically connected to each other at respective first ends thereof and separated from each other at respective second ends thereof; and a bipolar electrode installed between the terminal electrodes and electrically insulated the terminal electrodes.
Claims
1. A pipe-type electrolysis cell, comprising: a pair of terminal electrodes including an outer electrode and an inner electrode that are electrically connected to each other at respective first ends thereof and separated from each other at respective second ends thereof; and a pipe-type bipolar electrode installed between the terminal electrodes and electrically insulated from the terminal electrodes.
2. The pipe-type electrolysis cell according to claim 1, further comprising: an insulation unit supporting the separated second ends of the terminal electrodes; and a spiral block combined with the connected first ends of the terminal electrodes and provided with a spiral guide hole through which a fluid passes.
3. The pipe-type electrolysis cell according to claim 1, wherein the terminal electrodes include a connection plate that supports and connects the first ends of the inner electrode and the outer electrode, and which is provided with a fluid passing hole communicating with a channel formed between the inner electrode and the outer electrode, thereby guiding a fluid to the channel.
4. The pipe-type electrolysis cell according to claim 3, further comprising terminal insulating spacers provided to respective ends of the bipolar electrode to electrically insulate and space the bipolar electrode from the connection plate, the inner electrode, and the outer electrode.
5. The pipe-type electrolysis cell according to claim 1, wherein either one or both of an outside surface of the outer electrode having a pipe shape and an inside surface of the inner electrode having a pipe shape are plated with a metal having a high electrical conductivity, wherein the outside surface and the inside surface are not involved in an electrolytic reaction.
6. The pipe-type electrolysis cell according to claim 3, wherein the connection plate provided with the fluid passing hole, and the outer and inner electrodes are connected through welding.
7. The pipe-type electrolysis cell according to claim 3, wherein the fluid passing holes formed in the connection plate are aligned with spiral guide holes formed in the spiral block.
8. The pipe-type electrolysis cell according to claim 3, wherein a positioning guide pin is formed to protrude from an outside surface of the connection plate, the spiral block is combined with the outside surface of the connection plate, and the spiral block is provided with a plurality of spiral guide holes that are arranged in a circumferential direction so as to correspond to the fluid passing holes of the connection plate.
9. The pipe-type electrolysis cell according to claim 8, wherein the spiral block is provided with a positioning hole into which the positioning guide pin is inserted when the spiral block is combined with the connection plate such that the spiral guide holes are well aligned with the fluid passing holes of the connection plate.
10. The pipe-type electrolysis cell according to claim 2, wherein the insulation unit comprises: an outer insulating spacer provided on an outside surface of the bipolar electrode at a middle portion in a longitudinal direction; and an inner insulating spacer provided inside the bipolar electrode at the middle portion in the longitudinal direction.
11. The pipe-type electrolysis cell according to claim 3, further comprising: an insulation unit supporting and connecting the separated second ends of the terminal electrodes to each other; and a spiral block combined with the connected first ends of the terminal electrodes and provided with a spiral guide hole through which a fluid passes.
12. The pipe-type electrolysis cell according to claim 11, wherein the insulation unit comprises: an outer insulating spacer provided on an outside surface of the bipolar electrode at a middle portion in a longitudinal direction; and an inner insulating spacer provided inside the bipolar electrode at the middle portion in the longitudinal direction.
13. The pipe-type electrolysis cell according to claim 10, wherein the outer insulating spacer comprises: a plurality of protrusions formed on an inside surface thereof and arranged at regular intervals in a circumferential direction thereof, at a middle portion in a longitudinal direction thereof, the protrusions being in contact with the outside surface of the middle electrode; and a pair of electrode connection portions that are provided at respective ends thereof and into which the outer electrodes are inserted, the electrode connection portions having an inner diameter larger than that of the middle portion of the outer insulating spacer such that an inside surface of the electrode connection portion and an inside surface of the middle portion of the outer insulating spacer form a step shape.
14. The pipe-type electrolysis cell according to claim 10, wherein the inner insulating spacer comprises: a plurality of protrusions arranged at a middle portion of the middle electrode in a longitudinal direction, arranged at regular intervals in a circumferential direction, and formed to protrude from an outside surface of the inner insulating spacer; and a pair of electrode connection portions provided at respective ends thereof and having an outer diameter smaller than that of the middle portion of the inner insulating spacer such that an outside surface of the electrode connection portion and the outside surface of the middle portion of the inner insulating spacer form a step form, in which the electrode connection portions are inserted into the inner electrodes.
15. The pipe-type electrolysis cell according to claim 1, further comprising: a connection pipe or a inlet/outlet connection nipple combined with the first ends of the terminal electrodes, and used to connect one of the pipe-type electrolysis cells to another pipe-type electrolysis cell, wherein the connection pipe or the inlet/outlet connection nipple is structured such that a bottom surface thereof is sloped upwards toward an end of the connection pipe or the inlet/outlet connection nipple.
Description
BRIEF DESCRIPTION OF DRAWINGS
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DETAILED DESCRIPTION
[0064] Hereinbelow, a pipe-type electrolysis cell according to one embodiment of the invention will be described with reference to the accompanying drawings.
[0065] With reference to
[0066] The pipe-type electrolysis cell 110 according to one embodiment invention includes a pair of terminal electrodes, a bipolar electrode, an insulation unit, and a spiral block 118.
[0067] Herein, the pair of terminal electrodes includes inner electrodes 115a and 115b, outer electrodes 114a and 114b, and connection plates 116 by which first ends of the inner electrodes 115a and 115b are electrically connected to first ends of the outer electrodes 114a and 114b.
[0068] The bipolar electrode includes a pipe-type middle electrode 111 installed between the inner electrodes 115a and 115b and the outer electrodes 114a and 114b.
[0069] That is, the middle electrode 111 is a bipolar electrode having opposite polarities at opposite sides thereof. As shown in
[0070] The insulation unit includes an outer insulating spacer 112 installed outside the middle electrode 111, at a middle portion of the middle electrode 111 in a longitudinal direction thereof, and an inner insulating spacer 113 installed inside the middle portion at the middle portion. A further detailed description of the insulation will be given later.
[0071] The outer electrodes 114a and 114b have a pipe shape. One outer electrode (114a) of the outer electrodes serves as a cathode and the other outer electrode (114b) serves as an anode. The outer insulating spacer 112 is provided between the outer electrode 114a and the outer electrode 114b to electrically insulate the outer electrodes 114a and 114b from each other and spaces the outer electrodes 114a and 114b from the middle electrode 111. As illustrated in
[0072] As described above, adjacent ends (second ends) of the outer electrodes 114a and 114b are assembled with the outer insulating spacer 112, and the other ends (first ends) are respectively assembled with the connection pipes 120 or the inlet/outlet connection nipples 130.
[0073] In addition, the first ends of the outer electrodes 114a and 114b are connected to first ends of the inner electrodes 115a and 115b by the connection plates 116. The connection plates 116 are made of a metal. The first ends of the inner electrodes 115a and 115b and the first ends of the outer electrodes 114a and 114b are connected through a connection method such as welding that does not increase electrical resistance. Therefore, as to the inner electrodes 115a and 115b and the outer electrodes 114a and 114b connected by the connection plate 116, the outer electrode 114a and the inner electrode 115a, connected to each other, have the same polarity (i.e. both serving as a cathode) and the outer electrode 114b and the inner electrode 115b have the same polarity (i.e. both serving as an anode).
[0074] The inner insulating spacer 113 is provided between the inner electrodes 115a and 115b, so that the inner electrodes 115a and 115b are electrically insulated from each other by the inner insulating spacer 113. The inner insulating spacer 113 also spaces and electrically insulates the inner electrodes 115a and 115b from the middle electrode 111.
[0075] Herein, the inner insulating spacer 113 is installed at a middle portion inside the middle electrode 111 and is provided with a plurality of protrusions 113 on the outside surface thereof. The protrusions 113a protrude from the outside surface 113 of the inner insulating spacer 113 and are arranged at regular intervals in the circumferential direction. The protrusions 113 are in contact with the inside surface of the middle electrode 111. Respective ends of the inner insulating spacer 113 are provided with inner electrode connection portions 113b that have a smaller outer diameter than that of a middle portion of the inner insulating spacer 113 such that the outside surface of the inner electrode connection portion 113b and the outside surface of the middle portion of the inner insulating spacer 113 form a step shape. Therefore, the inner electrode connection portions 113b of the inner insulating spacer 113 can be respectively inserted into the adjacent ends of the inner electrodes 115a and 115b. The inner insulating spacer 113 supports the inner electrodes 115a and 115b while electrically insulating the inner electrodes 115a and 115b from each other, and also spaces and electrically insulates the inner electrodes 115a and 115b from the middle electrode 111.
[0076] The structures of the outer insulating spacer 112 and the inner insulating spacer 113 are not limited to those described above. The outer insulating spacer 112 and the inner insulating spacer 113 may have any structure that can meet requirements that the outer electrodes 114a and 114b can be supported in a state of being electrically insulated from each other, the inner electrodes 115a and 115b can be supported in a state of being electrically insulated from each other, and the outer electrodes and the inner electrodes can be spaced and electrically insulated from the middle electrode 111 by a predetermined distance. In this case, the protrusions 112a of the outer insulating spacer 112 and the protrusions 113a of the inner insulating spacer 113, which are provided to space and electrically insulate the outer electrodes and the inner electrodes from the middle electrode 111, are preferably configured not to impede the flow of an electrolyte solution which flows along a channel provided between the outer electrode and the middle electrode and a channel provided between the inner electrode and the middle electrode.
[0077] According to the structure described above, power is oppositely supplied to the bipolar electrode, i.e. the pipe-type middle electrode 11, which is disposed between and spaced from the outer electrodes 114a and 114b and the inner electrodes 115a and 115b, with respect to the outer electrodes 114a and 114b and the inner electrodes 115a and 115b. Accordingly, an electrolytic reaction occurs in a state in which a fluid flows along the outside surface and the inside surface of the middle electrode 111. Since the electrolytic reaction occurs while the fluid is flowing along the outside surface and the inside surface of the middle electrode 111, the pipe-type electrolysis cell of the present invention exhibits electrolysis performance that is twice or more than that of conventional pipe-type electrolysis cells. That is, with the same volume as a conventional pipe-type electrolysis cell, the pipe-type electrolysis cell of the invention can obtain two times higher electrolysis efficiency than the conventional pipe-type electrolysis cell. Since those skilled in the art can easily understand the detailed structure and operation of the pipe-type electrolysis cell, there will be no further description thereof.
[0078] In addition, the connection plate 116 is provided with a plurality of fluid passing holes 116a that are equal in size and are arranged at regular intervals in a circumferential direction of the connection plate 116 such that the fluid can be introduced into a gap between the inner electrodes 115a and 115b and the outer electrodes 114a and 114b. In addition, one or more positioning guide pins 116b are formed to protrude from the outside surface of the connection plate 116. The positioning guide pins 116b are configured to enable a combined structure of the electrodes to be precisely and accurately aligned with the spiral block 118 when the combined structure of the electrodes is combined with the spiral block.
[0079] In addition, the connection plate 116 may be made of a plurality of plates arranged in multiple stages. In this case, the plates are stacked such that the fluid passing holes provided to each plate are misaligned. That is, a fluid path extending through the fluid passing holes of the plates may form a spiral shape. Alternatively, each fluid passing hole 116a may extend in a spiral form in the connection plate 116, thereby guiding the fluid along a spiral flow path.
[0080] The spiral block 118 is connected to the outside surface of the connection plate 116. The spiral block 118 is provided with a plurality of spiral guide holes 118a that are arranged at intervals in a circumferential direction of the spiral block 118. Since the fluid spirally flows while passing through the spiral guide holes 118a, velocity distribution of the fluid can be uniformized. In addition, the spiral block 118 is provided with a positioning hole 118b that is used to position the spiral block 118 such that the guide holes 118a of the spiral block 118 can be precisely and accurately aligned with the fluid passing holes 116a of the connection plate 116 when the spiral block 118 is connected to the connection plate 116. When the positioning guide pin 116b of the connection plate 116 is inserted into the positioning hole 118b, the fluid passing holes 116a are automatically aligned with the guides hole 118a. Therefore, the fluid can flow without flow resistance. The spiral block 118 is assembled with the connection pipe 120 or the inlet/outlet connection nipple 130.
[0081] In addition, as to the middle electrode 111, a half of each of the outside surface and the inside surface in terms of the longitudinal direction is coated with an anode material. That is, both of the outside surface and the inside surface of the middle electrode 111 can be used for an electrolytic reaction unlike conventional arts. Therefore, electrolysis capacity is doubled.
[0082] In addition, among the terminal electrodes, the outer electrode 114a serving as the cathode and the inner electrode 115a serving as the cathode are made of stainless steel or nickel alloys. The outer electrode 114a and the inner electrode 115a serving as the cathode are connected to the connection plate 116 through a connection method such as welding that does not increase electric resistance. In addition, one or more surfaces of the electrodes, which do not participate in an electrolytic reaction while the electrolyte solution flows, for example, the inside surface of the inner electrode 115a or the outside surface of the outer electrode 114a, are preferably coated with a metal having a high electric conductivity, which uniformly distributes current intensity over the entire length of the electrode during the electrolytic reaction. For this reason, uniformity and efficiency of the electrolytic reaction can be improved compared with conventional multi-stage electrolytic cells, and heat generated during the electrolytic reaction can be controlled.
[0083] In addition, among the terminal electrodes, the outer electrode 114b and the inner electrode 115b serving as the anode are made of titanium. The inside surface of the outer electrode 114a and the outside surface of the inner electrode 115b are coated with a platinum oxide to form insoluble electrodes. Furthermore, these electrodes are plated and welded in the same manner as the electrodes serving as the cathode described above, thereby maintaining the electrical conductivity.
[0084] A plurality of pipe-type electrolysis cells 110 having the structure described above are arranged in series, and adjacent ends thereof are connected to each other by the connection pipe 120 so that a fluid can flow from one cell to another.
[0085] In addition, among the plurality of pipe-type electrolysis cells 110, the outermost electrolysis cells 110 are connected to the inlet/outlet connection nipples 130. That is, outer ends of both of the outermost pipe-type electrolysis cell 110 are connected to the connection pipes 120 or the inlet/outlet connection nipples 130.
[0086] Alternatively, the outer end of one of the outermost pipe-type electrolysis cells 110 may be connected to the connection pipe 120 and the outer end of the other of the outermost pipe-type electrolysis cells 110 may be connected to the inlet/outlet connection nipple 130.
[0087] In at least either one of the connection pipe 120 and the inlet/outlet connection nipple 130, an internal fluid channel, i.e. fluid passage channel, has a tapered form so that movement of fluid and separation of hydrogen are facilitated. That is, the connection pipe 120 and/or the inlet/outlet connection nipple 130 have bottom surfaces 121 and 131 that are sloped upward toward the outer ends thereof as shown in
[0088] As described above, an electrolysis unit module 100 is made up of the plurality of pipe-type electrolysis cells 110 connected in series with each other.
[0089] As described above, the pipe-type electrolysis cell 110 according to the embodiment of the invention is structured such that the pipe-type bipolar electrode (i.e. middle electrode) is arranged between the terminal electrodes consisting of the outer electrode and the inner electrode, thereby enabling the electrolytic reaction to occur on both the inside surface and the outside surface of the bipolar electrode. In this way, an amount of electrolytic reactions that was performed by two conventional electrolysis modules can be performed by one electrolysis module. That is, according to the present invention, the pipe-type electrolysis cell can obtain an electrolysis performance equal to that of a conventional pipe-type electrolysis cell even while being only half the size. In addition, according to the invention, the amount of electrode material is reduced to about 65%, and the amount of epoxy molding material and the amount of frames are also reduced by about 50%. That is, the pipe-type electrolysis cell of the invention is considerably more cost effective because it is possible to reduce the size and the material cost while maintaining electrolysis capacity.
[0090] In the case in which an electrolysis module made up of the pipe-type electrolysis cells having the structure described above is applied to a ship, it can be installed in old ships as well as new ships because it requires a reduced installation space.
[0091] The pipe-type electrolysis cell of the present invention can be applied to an electrolysis apparatus that can electrolyze general water such as flesh water as well as an electrolysis apparatus that electrolyzes sea water, salt water, and so on.
[0092] Although the preferred embodiment of the present invention has been disclosed for illustrative purposes, those skilled in the art will appreciate that various modifications, additions and substitutions are possible, without departing from the scope and spirit of the invention as disclosed in the accompanying claims.