Electrolysis cell and electrolysis tank
Provided is an electrolysis cell capable of suppressing the degradation of a cathode by the reverse current at the time of stopping electrolysis. According to an aspect of the invention, there is provided an electrolysis cell comprising an anode chamber, a cathode chamber, a partition wall separating the anode chamber from the cathode chamber, an anode installed in the anode chamber, a cathode installed in the cathode chamber, and a reverse current absorbing body having a substrate and a reverse current absorbing layer formed on the substrate and installed in the cathode chamber, in which the anode and the cathode are electrically connected and the cathode and the reverse current absorbing layer are electrically connected.
1. An electrolysis cell comprising:
an anode chamber;
a cathode chamber;
a partition wall separating the anode chamber from the cathode chamber;
an anode installed in the anode chamber;
a cathode installed in the cathode chamber; and
a reverse current absorbing body having a substrate and a reverse current absorbing layer formed on the substrate and installed in the cathode chamber,
wherein the anode and the cathode are electrically connected and the cathode and the reverse current absorbing layer are electrically connected, and
wherein the reverse current absorbing layer is a porous layer including Ni or NiO, and a full width at half maximum of a diffraction line peak of Ni metal at a diffraction angle 2θ=44.5° in a powder X-ray diffraction pattern of the reverse current absorbing layer is 0.6° or less.
2. The electrolysis cell according to claim 1 , wherein the reverse current absorbing layer includes an element having an oxidation-reduction potential lower than the cathode.
3. The electrolysis cell according to claim 1 , wherein the reverse current absorbing layer includes one or more kinds of elements selected from the group consisting of C, Cr, Ni, Ti, Fe, Co, Cu, Al, Zr, Ru, Rh, Pd, Ag, W, Re, Os, Ir, Pt, Au, Bi, Cd, Hg, Mn, Mo, Sn, Zn, La, Ce, Pr, Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, and Lu.
4. The electrolysis cell according to any one of claims 1 to 3 , wherein a pore volume of a pore having a pore size of 10 nm or greater is 80% or more of a total pore volume in a pore size distribution curve of the reverse current absorbing layer measured by a nitrogen gas adsorption method.
5. The electrolysis cell according to any one of claims 1 to 3 , wherein the reverse current absorbing layer is formed by thermal spraying Ni or NiO on at least a part of a surface of the substrate.
6. The electrolysis cell according to claim 5 , wherein the reverse current absorbing layer is formed by thermal spraying NiO on at least a part of a surface of the substrate and then performing a reduction treatment to the NiO.
7. The electrolysis cell according to any one of claims 1 to 3 , wherein the cathode has a Ni substrate and a catalytic layer formed on the Ni substrate.
8. The electrolysis cell according to any one of claims 1 to 3 , wherein
the cathode chamber further has a current collector, a support supporting the current collector, and a metal elastic body,
the metal elastic body is disposed between the current collector and the cathode,
the support is disposed between the current collector and the partition wall, and
the partition wall, the support, the current collector, the metal elastic body, and the cathode are electrically connected.
9. The electrolysis cell according to claim 8 , wherein
at least a part of the substrate of the reverse current absorbing body is the current collector, and
the reverse current absorbing layer is formed on a surface of the current collector.
10. The electrolysis cell according to claim 8 , wherein
at least a part of the substrate of the reverse current absorbing body is the metal elastic body, and
the reverse current absorbing layer is formed on a surface of the metal elastic body.
11. The electrolysis cell according to claim 8 , wherein
at least a part of the substrate of the reverse current absorbing body is the partition wall, and
the reverse current absorbing layer is formed on a surface of the partition wall.
12. The electrolysis cell according to claim 8 , wherein
at least a part of the substrate of the reverse current absorbing body is the support, and
the reverse current absorbing layer is formed on a surface of the support.
13. The electrolysis cell according to claim 8 , wherein
at least a part of the reverse current absorbing body is disposed between the cathode and the metal elastic body.
14. The electrolysis cell according to claim 8 , wherein
at least a part of the reverse current absorbing body is disposed between the metal elastic body and the current collector.
15. The electrolysis cell according to claim 8 , wherein
at least a part of the reverse current absorbing body is disposed between the current collector and the partition wall.
16. The electrolysis cell according to any one of claims 1 to 3 , wherein
the cathode chamber further has a support supporting the cathode,
the support is disposed between the cathode and the partition wall, and
the partition wall, the support, and the cathode are electrically connected.
17. The electrolysis cell according to claim 16 , wherein
at least a part of the substrate of the reverse current absorbing body is the partition wall, and
the reverse current absorbing layer is formed on a surface of the partition wall.
18. The electrolysis cell according to claim 17 , wherein
at least a part of the substrate of the reverse current absorbing body is the support, and
the reverse current absorbing layer is formed on a surface of the support.
19. The electrolysis cell according to claim 18 , wherein the reverse current absorbing body is disposed between the cathode and the partition wall.
20. The electrolysis cell according to claim 17 , wherein the reverse current absorbing body is disposed between the cathode and the partition wall.
21. The electrolysis cell according to claim 16 , wherein
at least a part of the substrate of the reverse current absorbing body is the support, and
the reverse current absorbing layer is formed on a surface of the support.
22. The electrolysis cell according to claim 21 , wherein the reverse current absorbing body is disposed between the cathode and the partition wall.
23. The electrolysis cell according to claim 16 , wherein the reverse current absorbing body is disposed between the cathode and the partition wall.
24. The electrolysis cell according to any one of claims 1 to 3 , wherein at least a part of the substrate of the reverse current absorbing body is a cube, a cuboid, a plate shape, a rod shape, a reticular shape, or a spherical shape.
25. The electrolysis cell according to any one of claims 1 to 3 , wherein a specific surface area of the reverse current absorbing layer is from 0.01 to 100 m 2 /g.
26. The electrolysis cell according to any one of claims 1 to 3 , wherein a sum of electric quantities absorbed by all of the reverse current absorbing bodies is from 1,000 to 2,000,000 C/m 2 .
27. The electrolysis cell according to any one of claims 1 to 3 , wherein a sum of effective surface areas of all of the reverse current absorbing bodies is from 10 to 100,000 m 2 .
28. An electrolysis tank comprising the electrolysis cell according to any one of claims 1 to 3 .
29. The electrolysis cell according to claim 2 , wherein the reverse current absorbing layer includes one or more kinds of elements selected from the group consisting of C, Cr, Ni, Ti, Fe, Co, Cu, Al, Zr, Ru, Rh, Pd, Ag, W, Re, Os, Ir, Pt, Au, Bi, Cd, Hg, Mn, Mo, Sn, Zn, La, Ce, Pr, Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, and Lu.
30. The electrolysis cell according to claim 29 , wherein a pore volume of a pore having a pore size of 10 nm or greater is 80% or more of a total pore volume in a pore size distribution curve of the reverse current absorbing layer measured by a nitrogen gas adsorption method.
31. The electrolysis cell according to claim 29 , wherein the reverse current absorbing layer is formed by thermal spraying Ni or NiO on at least a part of a surface of the substrate.
32. The electrolysis cell according to claim 29 , wherein the reverse current absorbing layer is formed by thermal spraying NiO on at least a part of a surface of the substrate and then performing a reduction treatment to the NiO.
33. The electrolysis cell according to claim 29 , wherein the cathode has a Ni substrate and a catalytic layer formed on the Ni substrate.
34. The electrolysis cell according to claim 29 , wherein
the cathode chamber further has a current collector, a support supporting the current collector, and a metal elastic body,
the metal elastic body is disposed between the current collector and the cathode,
the support is disposed between the current collector and the partition wall, and
the partition wall, the support, the current collector, the metal elastic body, and the cathode are electrically connected.
35. The electrolysis cell according to claim 34 , wherein
at least a part of the substrate of the reverse current absorbing body is the current collector, and
the reverse current absorbing layer is formed on a surface of the current collector.
36. The electrolysis cell according to claim 34 , wherein at least a part of the substrate of the reverse current absorbing body is the metal elastic body, and
the reverse current absorbing layer is formed on a surface of the metal elastic body.
37. The electrolysis cell according to claim 34 , wherein
at least a part of the substrate of the reverse current absorbing body is the partition wall, and
the reverse current absorbing layer is formed on a surface of the partition wall.
38. The electrolysis cell according to claim 34 , wherein
at least a part of the substrate of the reverse current absorbing body is the support, and the reverse current absorbing layer is formed on a surface of the support.
39. The electrolysis cell according to claim 34 , wherein
at least a part of the reverse current absorbing body is disposed between the cathode and the metal elastic body.
40. The electrolysis cell according to claim 34 , wherein at least a part of the reverse current absorbing body is disposed between the metal elastic body and the current collector.
41. The electrolysis cell according to claim 34 , wherein
at least a part of the reverse current absorbing body is disposed between the current collector and the partition wall.
42. The electrolysis cell according to claim 29 , wherein
the cathode chamber further has a support supporting the cathode,
the support is disposed between the cathode and the partition wall, and
the partition wall, the support, and the cathode are electrically connected.
43. The electrolysis cell according to claim 42 , wherein
at least a part of the substrate of the reverse current absorbing body is the partition wall, and
the reverse current absorbing layer is formed on a surface of the partition wall.
44. The electrolysis cell according to claim 43 , wherein
at least a part of the substrate of the reverse current absorbing body is the support, and
the reverse current absorbing layer is formed on a surface of the support.
45. The electrolysis cell according to claim 44 , wherein the reverse current absorbing body is disposed between the cathode and the partition wall.
46. The electrolysis cell according to claim 43 , wherein the reverse current absorbing body is disposed between the cathode and the partition wall.
47. The electrolysis cell according to claim 42 , wherein
at least a part of the substrate of the reverse current absorbing body is the support, and
the reverse current absorbing layer is formed on a surface of the support.
48. The electrolysis cell according to claim 47 , wherein the reverse current absorbing body is disposed between the cathode and the partition wall.
49. The electrolysis cell according to claim 42 , wherein the reverse current absorbing body is disposed between the cathode and the partition wall.
50. The electrolysis cell according to claim 29 , wherein
at least a part of the substrate of the reverse current absorbing body is a cube, a cuboid, a plate shape, a rod shape, a reticular shape, or a spherical shape.
51. The electrolysis cell according to claim 29 , wherein a specific surface area of the reverse current absorbing layer is from 0.01 to 100 m 2 /g.
52. The electrolysis cell according to claim 29 , wherein a sum of electric quantities absorbed by all of the reverse current absorbing bodies is from 1,000 to 2,000,000 C/m 2 .
53. The electrolysis cell according to claim 29 , wherein
a sum of effective surface areas of all of the reverse current absorbing bodies is from 10 to 100,000 m 2 .
54. An electrolysis tank comprising the electrolysis cell according to claim 29 .