DUAL-MEMBRANE ON-LINE GENERATOR FOR ACID OR ALKALI SOLUTION

Abstract

A dual-membrane on-line generator for an acid or alkali solution is provided, including an upper electrolytic cell body (3), a middle electrolytic cell body (4) and a lower electrolytic cell body (5) which are clamped by an upper fastening steel plate (1) and a lower fastening steel plate (2), an upper regeneration liquid channel (A), a middle eluent channel (B) and a lower regeneration liquid channel (C) being provided on the middle electrolytic cell body (4).

Claims

1. A dual-membrane on-line generator for an acid or alkali solution, comprising an upper fastening steel plate (1), a lower fastening steel plate (2), an upper electrolytic cell body (3), a middle electrolytic cell body (4) and a lower electrolytic cell body (5), wherein the upper electrolytic cell body (3), the middle electrolytic cell body (4) and the lower electrolytic cell body (5) are clamped in sequence by the upper fastening steel plate (1) and the lower fastening steel plate (2), and upper and lower corners of the upper fastening steel plate (1) and the lower fastening steel plate (2) are fastened with fastening screws (11); wherein, an upper regeneration liquid channel (A), a middle eluent channel (B) and a lower regeneration liquid channel (C) are arranged on the middle electrolytic cell body (4); two openings are provided on both sides of the upper regeneration liquid channel (A), and are respectively used as an upper regeneration liquid channel inlet (14) and an upper regeneration liquid channel outlet (15), and openings of the upper regeneration liquid channel inlet (14) and the upper regeneration liquid channel outlet (15) are respectively arranged on the upper fastening steel plate (1), a cathode electrode (12) is arranged in the upper regeneration liquid channel (A), and the other end of the cathode electrode (12) is arranged on the upper fastening steel plate (1); the middle eluent channel (B) is a hollow channel, two openings are provided on both sides of the middle eluent channel (B), and are respectively used as a middle eluent channel inlet (16) and a middle eluent channel outlet (17), and openings of the middle eluent channel inlet (16) and the middle eluent channel outlet (17) are respectively arranged on both sides of the middle electrolytic cell body (4); two openings are provided on both sides of in the lower regeneration liquid channel (C), and are respectively used as a lower regeneration liquid channel inlet (18) and a lower regeneration liquid channel outlet (19), and openings of the lower regeneration liquid channel inlet (18) and the lower regeneration liquid channel outlet (19) are respectively arranged on the lower fastening steel plate (2), an anode electrode (13) is arranged in the lower regeneration liquid channel (C), and the other end of the anode electrode (13) is arranged on the lower fastening steel plate (2); a porous cathode sheet (6), a first cation exchange membrane (701) and a bipolar membrane (8) are provided between the upper regeneration liquid channel (A) and the middle eluent channel (B); a porous anode sheet (10) and a second cation exchange membrane (702) are provided between the middle eluent channel (B) and the lower regeneration liquid channel (C); upstream pure water enters through the middle eluent channel inlet (16), and flows out from the middle eluent channel outlet (17) after passing through the middle eluent channel (B); pure alkali regeneration liquid enters through the upper regeneration liquid channel inlet (14), and flows out from the upper regeneration liquid channel outlet (15) after passing through the upper regeneration liquid channel (A), and then enters through the lower regeneration liquid channel inlet (18), flows out from the lower regeneration liquid channel outlet (19) after passing through the lower regeneration liquid channel (C), and flows back to regeneration liquid.

2. The dual-membrane on-line generator for an acid or alkali solution according to claim 1, wherein the middle eluent channel (B) is filled with ion exchange screens (9) or inert particles with a wide pH working range or monolithic columns or fibers.

3. The dual-membrane on-line generator for an acid or alkali solution according to claim 1, wherein multi-layer and overlapping first cation exchange membranes (701) and bipolar membranes (8) are provided between the upper regeneration liquid channel (A) and the middle eluent channel (B).

4. The dual-membrane on-line generator for an acid or alkali solution according to claim 1, wherein multi-layer and overlapping second cation exchange membranes (702) are provided between the middle eluent channel (B) and the lower regeneration liquid channel (C).

5. The dual-membrane on-line generator for an acid or alkali solution according to claim 3, wherein the first cation exchange membrane (701), the second cation exchange membrane (702) and the bipolar membrane are in form of ion exchange plate membranes.

6. The dual-membrane on-line generator for an acid or alkali solution according to claim 1, wherein the cathode electrode (12) and the anode electrode (13) adopt a porous platinum electrode structure.

7. A dual-membrane on-line generator for an acid or alkali solution, comprising an upper fastening steel plate (1), a lower fastening steel plate (2), an upper electrolytic cell body (3), a middle electrolytic cell body (4) and a lower electrolytic cell body (5), wherein the upper electrolytic cell body (3), the middle electrolytic cell body (4) and the lower electrolytic cell body (5) are clamped in sequence by the upper fastening steel plate (1) and the lower fastening steel plate (2), and upper and lower corners of the upper fastening steel plate (1) and the lower fastening steel plate (2) are fastened with fastening screws (11); wherein, an upper regeneration liquid channel (A), a middle eluent channel (B) and a lower regeneration liquid channel (C) are arranged on the middle electrolytic cell body (4); two openings are provided on both sides of the upper regeneration liquid channel (A), and are respectively used as an upper regeneration liquid channel inlet (14) and an upper regeneration liquid channel outlet (15), and openings of the upper regeneration liquid channel inlet (14) and the upper regeneration liquid channel outlet (15) are respectively arranged on the upper fastening steel plate (1), an anode electrode (13) is arranged in the upper regeneration liquid channel (A), the anode electrode (13) adopts a porous platinum electrode structure, and the other end of the anode electrode (13) is arranged on the upper fastening steel plate (1); the middle eluent channel (B) is a hollow channel, two openings are provided on both sides of the middle eluent channel (B), and are respectively used as a middle eluent channel inlet (16) and a middle eluent channel outlet (17), and openings of the middle eluent channel inlet (16) and the middle eluent channel outlet (17) are respectively arranged on both sides of the middle electrolytic cell body (4); two openings are provided on both sides of in the lower regeneration liquid channel (C), and are respectively used as the lower regeneration liquid channel inlet (18) and the lower regeneration liquid channel outlet (19), and openings of the lower regeneration liquid channel inlet (18) and the lower regeneration liquid channel outlet (19) are respectively arranged on the lower fastening steel plate (2), a cathode electrode (12) is provided in the lower regenerating solution channel (C), the cathode electrode (12) adopts a porous platinum electrode structure, and the other end is arranged on the lower fastening steel plate (2); a porous anode sheet (10), a first anion exchange membrane (703) and a bipolar membrane (8) are provided between the upper regeneration liquid channel (A) and the middle eluent channel (B); a porous cathode sheet (6) and a second anion exchange membrane (704) are provided between the middle eluent channel (B) and the lower regeneration liquid channel (C); upstream pure water enters through the middle eluent channel inlet (16), and flows out from the middle eluent channel outlet (17) after passing through the middle eluent channel (B); pure acid regeneration liquid enters through the upper regeneration liquid channel inlet (14), and flows out from the upper regeneration liquid channel outlet (15) after passing through the upper regeneration liquid channel (A), and then enters through the lower regeneration liquid channel inlet (18), flows out from the lower regeneration liquid channel outlet (19) after passing through the lower regeneration liquid channel (C), and flows back to regeneration liquid.

8. The dual-membrane on-line generator for an acid or alkali solution according to claim 7, wherein the middle eluent channel (B) is filled with ion exchange screens (9) or inert particles with a wide pH working range or monolithic columns or fibers.

9. The dual-membrane on-line generator for an acid or alkali solution according to claim 7, wherein multi-layer and overlapping first anion exchange membranes (703) and bipolar membranes (8) are provided between the upper regeneration liquid channel (A) and the middle eluent channel (B).

10. The dual-membrane on-line generator for an acid or alkali solution according to claim 7, wherein multi-layer and overlapping second anion exchange membranes (704) are provided between the middle eluent channel (B) and the lower regeneration liquid channel (C).

Description

BRIEF DESCRIPTION OF DRAWINGS

[0020] FIG. 1 is a schematic structural diagram of a dual-membrane on-line generator for an acid or alkali solution of Embodiment 1 of the present invention.

[0021] FIG. 2 is a schematic diagram of a working principle of a dual-membrane on-line generator for an acid or alkali solution of Embodiment 1 of the present invention.

[0022] FIG. 3 shows a correlation between a current and a concentration of KOH generated by a dual-membrane on-line generator for an alkali solution of Embodiment 1 of the present invention.

[0023] FIG. 4 is a schematic structural diagram of a dual-membrane on-line generator for an acid or alkali solution of Embodiment 3 of the present invention.

[0024] FIG. 5 is a schematic diagram of operation repeatability for acid generation of a dual-membrane on-line generator for an acid solution of Embodiment 3 of the present invention.

[0025] Reference signs in the figures are as follows: [0026] A. Upper regeneration liquid channel, B. Middle eluent channel; [0027] C. Lower regeneration liquid channel; [0028] 1. Upper fastening steel plate; 2. Lower fastening steel plate; [0029] 3. Upper electrolytic cell body; 4. Middle electrolytic cell body; [0030] 5. Lower electrolytic cell body; 6. Porous cathode sheet; [0031] 701. First cation exchange membrane; 702. Second cation exchange membrane; [0032] 703. First anion exchange membrane; 704. Second anion exchange membrane; [0033] 8. Bipolar membrane 9. Ion exchange screen; [0034] 10. Porous anode sheet; 11. Fastening screw; [0035] 12. Cathode electrode; 13. Anode electrode; [0036] 14. Upper regeneration liquid channel inlet; 15. Upper regeneration liquid channel outlet; [0037] 16. Middle eluent channel inlet; 17. Middle eluent channel outlet; [0038] 18. Lower regeneration liquid channel inlet; 19. Lower regeneration liquid channel outlet.

DETAILED DESCRIPTION OF EMBODIMENTS

[0039] The specific embodiments of the dual-membrane on-line generator for an acid or alkali solution of the present invention are explained in detail below with reference to the accompanying drawings. It should be noted that the embodiments of the present invention is not limited to the following embodiments. In addition, the experimental methods used in the embodiments are conventional methods unless otherwise specified. Similarly, the materials, structures, reagents, etc. used in the embodiments are all commercially available unless otherwise specified.

Embodiment 1

[0040] Referring to FIG. 1, a dual-membrane on-line generator for an acid or alkali solution is provided. In this solution, an on-line generator for an alkali solution is provided, including: an upper fastening steel plate 1, a lower fastening steel plate 2, an upper electrolytic cell body 3, a middle electrolytic cell body 4, and a lower electrolytic cell body 5. The upper electrolytic cell body 3, the middle electrolytic cell body 4, and the lower electrolytic cell body 5 are clamped in sequence by the upper fastening steel plate 1 and the lower fastening steel plate 2, and upper and lower corners of the upper fastening steel plate 1 and the lower fastening steel plate 2 are fastened with fastening screws 11. This is a connection form of an overall structure. However, the following operations need to be done prior to this.

[0041] The middle electrolytic cell body 4 is provided with an upper regeneration liquid channel A, a middle eluent channel B, and a lower regeneration liquid channel C. Two openings are provided on both sides of the upper regeneration liquid channel A, and are respectively used as an upper regeneration liquid channel inlet 14 and an upper regeneration liquid channel outlet 15. Openings of the upper regeneration liquid channel inlet 14 and the upper regeneration liquid channel outlet 15 can be respectively arranged on both sides of the upper fastening steel plate 1. Then, a cathode electrode 12 (corresponding to the anode electrode 13) is arranged in the upper regeneration liquid channel A, and the cathode electrode 12 may adopt a porous platinum electrode structure. One end of the cathode electrode 12 may be arranged in the middle of the upper fastening steel plate 1.

[0042] The middle eluent channel B can be a hollow channel, or the middle eluent channel B is filled with ion exchange screens 9 or inert particles with a wide pH working range or monolithic columns or fibers. Two openings are provided on both sides of the middle eluent channel B, and are respectively used as a middle eluent channel inlet 16 and a middle eluent channel outlet 17. Openings of the middle eluent channel inlet 16 and the middle eluent channel outlet 17 can be respectively arranged on both sides of the middle electrolytic cell body 4. In specific implementation, the middle eluent channel inlet 16 can be arranged on a left side of the middle electrolytic cell body 4, and the middle eluent channel outlet 17 is arranged on a right side of the middle electrolytic cell body 4 (shown based on an orientation of FIG. 1).

[0043] Two openings are provided on both sides of the lower regeneration liquid channel C, and are respectively used as a lower regeneration liquid channel inlet 18 and a lower regeneration liquid channel outlet 19. Openings of the lower regeneration liquid channel inlet 18 and the lower regeneration liquid channel outlet 19 are respectively provided on both sides of the lower fastening steel plate 2. Then, an anode electrode 13 (corresponding to the cathode electrode 12) is provided in the lower regeneration liquid channel C, and the anode electrode 13 adopts a porous platinum electrode structure. One end of the anode electrode 13 may be arranged in the middle of the lower fastening steel plate 2.

[0044] A porous cathode sheet 6, a first cation exchange membrane 701 and a bipolar membrane 8 are arranged layer by layer from the outside to the inside (shown based on the orientation of FIG. 1) between the upper regeneration liquid channel A and the middle eluent channel B.

[0045] A porous anode sheet 10 and a second cation exchange membrane 702 are arranged layer by layer from the outside to the inside (shown based on the orientation of FIG. 1) between the middle eluent channel B and the lower regeneration liquid channel C.

[0046] The first cation exchange membrane 701, the second cation exchange membrane 702, and the bipolar membrane 8 used in the embodiments of the present invention are all in form of ion exchange plate membranes.

[0047] The dual-membrane on-line generator for an alkali solution of Embodiment 1 is assembled according to the above steps and FIG. 1, and the middle eluent channel B and the two regeneration liquid channels (the upper regeneration liquid channel A and the lower regeneration liquid channel C) are independent from each other. This structure is used, so that the dual-membrane on-line generator for an alkali solution of Embodiment 1 does not generate eluent containing electrolytic gas. In this way, a concentration of an alkali solution is proportional to an applied current, and stability and repeatability are good.

[0048] A working mode of the dual-membrane on-line generator for an alkali solution of Embodiment 1 is (see FIG. 2) as follows: Upstream pure water enters through the middle eluent channel inlet 16, and flows out from the middle eluent channel outlet 17 after passing through the middle eluent channel B. Pure alkali (KOH) regeneration liquid enters through the upper regeneration liquid channel inlet 14, and flows out from the upper regeneration liquid channel outlet 15 after passing through the upper regeneration liquid channel A, and then enters through the lower regeneration liquid channel inlet 18, flows out from the lower regeneration liquid channel outlet 19 after passing through the lower regeneration liquid channel C, and flows back into regeneration liquid. The dual-membrane on-line generator for an alkali solution of Embodiment 1 utilizes spatial isolation of the bipolar membrane 8 from the electric field and the alkali solution, so that insufficient purity of the alkali solution due to insufficient stability thereof is avoided.

[0049] The correlation between the current and the alkali solution generated by the dual-membrane on-line generator for an alkali solution of Embodiment 1 is shown in FIG. 3. The dual-membrane on-line generator for an alkali solution of Embodiment 1 can online converts the pure water entering the eluent from the middle eluent channel inlet 16 into a KOH solution, and a concentration of the generated KOH solution is positively correlated with the current applied to the porous cathode sheet 6 and the porous anode sheet 10. It can be learned from FIG. 3 that the concentration of the generated KOH solution is linearly correlated with the applied current. Therefore, the concentration of the generated alkali solution can be conveniently controlled by controlling the current.

Embodiment 2

[0050] A dual-membrane on-line generator for an acid or alkali solution is provided, and a structure of the generator is basically the same as that in Embodiment 1. Differences are as follows:

[0051] Multi-layer and overlapping first cation exchange membranes 701 and bipolar membranes 8 are arranged layer by layer from the outside to the inside (shown based on the orientation of FIG. 1) between the upper regeneration liquid channel A and the middle eluent channel B.

[0052] Multi-layer and overlapping second cation exchange membranes 702 are arranged layer by layer from the outside to the inside (shown based on the orientation of FIG. 1) between the middle eluent channel B and the lower regeneration liquid channel C.

Embodiment 3

[0053] Referring to FIG. 4, a dual-membrane on-line generator for an acid or alkali solution is provided. In this solution, an on-line generator for an acid solution is provided, and a structure of the generator is basically the same as that in Embodiment 1. Differences are as follows: A porous anode sheet 10, a first anion exchange membrane 703, and a bipolar membrane 8 are arranged layer by layer from the outside to the inside (shown based on an orientation of FIG. 4) between the upper regeneration liquid channel A and the middle eluent channel B.

[0054] A porous cathode sheet 6 and a second anion exchange membrane 704 are arranged layer by layer from the outside to the inside (shown based on the orientation of FIG. 4) between the middle eluent channel B and the lower regeneration liquid channel C.

[0055] An anode electrode 13 (corresponding to the cathode electrode 12) is provided in the upper regeneration liquid channel A. A cathode electrode 12 (corresponding to the anode electrode 13) is provided in the lower regeneration liquid channel C.

[0056] Upstream pure water enters through the middle eluent channel inlet 16, and flows out from the middle eluent channel outlet 17 after passing through the middle eluent channel B. Pure acid regeneration liquid enters through the upper regeneration liquid channel inlet 14, and flows out from the upper regeneration liquid channel outlet 15 after passing through the upper regeneration liquid channel A, and then enters through the lower regeneration liquid channel inlet 18, flows out from the lower regeneration liquid channel outlet 19 after passing through the lower regeneration liquid channel C, and flows back to regeneration liquid.

[0057] The dual-membrane on-line generator for an acid solution of Embodiment 3 is assembled according to the steps of Embodiment 3 and FIG. 4, and the middle eluent channel B and the two regeneration liquid channels (the upper regeneration liquid channel A and the lower regeneration liquid channel C) are independent from each other. This structure is used, so that the dual-membrane on-line generator for an acid solution of Embodiment 3 does not generate eluent containing electrolytic gas. In this way, a concentration of the acid solution is proportional to an applied current, and stability and repeatability are good.

[0058] For the repeatability of generating an acid solution generated online by the dual-membrane on-line generator for an acid solution in Embodiment 3, refer to FIG. 5: A flow rate of pure water entering through the inlet 16 is controlled, and a current can be changed to obtain current-related acid solutions of different concentrations from the middle eluent channel outlet 17. Online measurement can be performed on the concentration of the acid solution by using a commercial conductivity detector (the conductivity detector can be purchased directly from commercial channels, does not belong to the scope of protection of the present invention, and is only used to indirectly evaluate the performance of the present invention, and therefore is not directly drawn herein). If different currents are applied between the porous cathode sheet 6 and the porous anode sheet 10, for example: 10 mA, 30 mA, and 50 mA, the acid solutions generated under different currents generate different signal values on the conductivity detector, but the signal values are almost the same under the same current. It can be learned from FIG. 5 that electrical conductivity detection values of the acid solution obtained by repeating the above current for three times are very consistent, and it indicates that the operation of the dual-membrane on-line generator for an acid solution of Embodiment 3 has good repeatability.

Embodiment 4

[0059] A dual-membrane on-line generator for an acid or alkali solution is provided, and a structure of the generator is basically the same as that in Embodiment 3. Differences are as follows:

[0060] Multi-layer and overlapping first anion exchange membranes 703 and bipolar membranes 8 are arranged layer by layer from the outside to the inside (shown based on the orientation of FIG. 4) between the upper regeneration liquid channel A and the middle eluent channel B.

[0061] Multi-layer and overlapping second anion exchange membranes 704 are arranged layer by layer from the outside to the inside (shown based on an orientation of FIG. 1) between the middle eluent channel B and the lower regeneration liquid channel C.

[0062] The above description is only the preferred embodiments of the present invention. It should be pointed out that for the person skilled in the art, several improvements and modifications can be made without departing from the principle and structure of the present invention. These improvements and modifications should also be regarded as the protection scope of the present invention.