Electrolytic cell

A filter-press type electrolytic cell comprises alternatively arranging quadrilateral frames and ion-exchange membranes to form alternatively anolyte compartments and catholyte compartments under fastening the frames wherein said frame comprises hollow member for path of liquid and gas which has inlet or outlet at the outer surface thereof and holes at the inner surface thereof and a gas-liquid separator whereby each type of electrolytes is passed into an anolyte or catholyte compartment formed in the frame and the electrolyzed product is discharged from the anolyte or catholyte compartment.

BACKGROUND OF THE INVENTION: 
1. Field of the Invention: 
The present invention relates to a filter-press type electrolytic cell 
formed by alternatively arranging the frames and the ion-exchange 
membranes and fastening them. 
More particularly, it relates to a filter-press type electrolytic cell for 
producing caustic alkali by an electrolysis of an aqueous alkali metal 
salt such as an alkali metal chloride. 
More particularly, it relates to a filter-press type electrolytic cell 
wherein a saturated solution of sodium chloride or like is fed into the 
anolyte compartment and water or a dilute solution of sodium hydroxide is 
fed into the catholyte compartment, and the electrolysis is attained to 
obtain chlorine and a dilute solution of sodium chloride from the anolyte 
compartment and to obtain a concentrated solution of sodium hydroxide (20 
to 40 wt.%) and hydrogen gas from the catholyte compartment. 
2. Description of the Prior Art: 
In the electrolytic cell which is one of the filter-press type electrolytic 
cells, the frames having an anode, the ion-exchange membranes and the 
frames having a cathode are alternatively arranged and fastened to form 
anolyte compartment and catholyte compartment which are respectively 
partitioned with the membrane. 
A solution should be fed and discharged through the frames for the 
electrolytic compartments such as the anolyte compartments and catholyte 
compartments, in the operation of electrolysis. 
The frames for the conventional electrolytic cell are formed by plates made 
of synthetic resin having a central opening and a plurality of surrounding 
holes so as to communicate the corresponding holes in alignment for the 
compartments in the case of arrangement and fastening of the frames and 
have groove for communicating the holes and the electrolytic compartments, 
as disclosed in U.S. Pat. No. 3,869,375; U.S. Pat. No. 3,017,338 and U.S. 
Pat. No 3,933,617. When the solution is fed to the electrolytic 
compartment or is discharged from it, the solution is passed into the 
holes communicating through the frames at the bottoms of the frames and is 
fed through the groove to the electrolytic compartments. The electrolyzed 
solution or gas is passed through the groove into the holes communicating 
through the frames at the upper parts of the frames and is discharged 
through the communicating holes. 
In order to form said grooves and holes on the frames, high processing 
accuracy and complicated processing operation are required and the work is 
not easy and the cost is expensive. 
It is disadvantages to use block type frames made of anticorrosive metal 
from the viewpoints expense and weight. 
In the ion-exchange membrane electrolysis, the heat is generated by the 
electric resistance of the solution and the ion-exchange membrane in the 
compartments during the electrolysis whereby the liquids in the 
compartments are heated to about 80.degree. to 120.degree. C. It is 
required to use the frames which are heat resistance to prevent the 
deformation. In the case of the ion-exchange membrane electrolytic cell, 
the frames made of the synthetic resin is not suitable, and the frames 
made of superior metal should be used. 
The frame of the filter-press type electrolytic cell using asbestos fabric 
has been known in U.S. Pat. No. 3,836,448. In the frame, the upper zone(2) 
for gas-liquid separation is formed at the upper part of the frame. The 
channels(5) are formed at the both side parts and lower part of the frame. 
The upper zone(2) is connected to the channels. 
As shown in FIG. 2, the electrolyte is fed from the compartment to the 
upper zone wherein the gas is separated and the liquid is recycled through 
the channel to the compartment. From the viewpoint of whole of the 
electrolytic cell, the saturated aqueous solution is fed into the anolyte 
compartment to be electrolyzed. The most of the solution is fed through 
the asbestos membrane into the catholyte compartment. From the catholyte 
compartment, an aqueous solution containing sodium hydroxide and sodium 
chloride is discharged. 
The channel(5) of the side part of the frame is fine. The circulation of 
the solution in the frame is not so large because of the pressure loss. 
The volume of the upper zone for the gas-liquid separation need not so 
large. However, in the ion-exchange membrane electrolytic cell, the 
feeding and discharging of the solution is attained in each compartment as 
described above. The product of the electrolysis is obtained from the 
upper parts of the compartments. Accordingly, when the frame is used as 
the frame for the ion-exchange membrane type electrolytic cell, the volume 
of the solution fed into the upper zone of the frame is increased in the 
comparison with the conventional asbestos diaphragm method. In order to 
attain suitable gas-liquid separation, the volume of the upper zone should 
be large. 
From the viewpoint of the strength of the upper zone of the frame, it is 
necessary to increase the thickness of the frame. Accordingly, when the 
conventional frames are used as the frames of the ion-exchange membrane 
type electrolytic cell, the size of the cell should be too large from the 
viewpoint of the characteristics. The frame should be made of a metal and 
the weight is too heavy. 
SUMMARY OF THE INVENTION: 
It is an object of the present invention to provide a filter-press type 
electrolytic cell having ion-exchange membranes which is easily processed 
and prepared and can be prepared with low cost and low weight. 
It is another object of the invention to provide a filter-press type 
electrolytic cell which comprises hollow members for path of liquid and 
gas in which a passage for liquid or gas is formed. 
It is the other object of the invention to provide a frame for an 
filter-press type cell for producing a caustic alkali by an electrolysis 
of an aqueous alkali metal salt. 
The objects of the invention have been attained to provide a filter-press 
type electrolytic cell which comprises alternatively arranging frames and 
ion-exchange membranes to form alternatively anolyte compartments and 
catholyte compartments under fastening the frames wherein said frame 
comprises hollow member for path of liquid and gas which has inlet or 
outlet at the outer surface thereof and holes at the inner surface thereof 
whereby each type of electrolytes is passed into an anolyte or catholyte 
compartment formed in the frame and the electrolyzed product is discharged 
from the anolyte or catholyte compartment.

DETAILED DESCRIPTION OF THE EMBODIMENTS: Detailed 
Referring to the drawings, the frame of the invention will be illustrated. 
It is preferable to fasten the frames and the ion-exchange membrane through 
a gasket so as to improve the sealing between the frame and the 
ion-exchange membrane for the electrolytic cell. The fastening pressure is 
preferably 1-20 Kg/cm.sup.2 especially 2-10 Kg/cm.sup.2 by unit area of 
frame. It is preferable to use hollow members having a regular square 
sectional view shown in FIG. 2(a) as the frames (1) from the viewpoint of 
easy assemble, though it is possible to use the hollow members having the 
other sectional views shown in FIGS. 2(b) to (f). The hollow member shown 
in FIG. 2(bis rectangular sectional view; 
The sectional views of the hollow members are FIG. 2(b) of rectangule; 
FIG. 2(c) of circle; and FIG. 2(d) of ellipse. 
When the section is about round shape as FIGS. 2(c) and (d), the seal 
pressure can be centralized to attain high sealing effect in the case of 
holding the diaphragm through the gasket by the frames. 
In the embodiment of FIG. 2(e), each groove is formed on each corresponding 
side surfaces. A gasket of O-ring shape can be disposed in the groove. The 
diaphragm can be firmly held by putting the diaphragm between the frames 
and fastening them. 
In the embodiment of FIG. 2(f), each W shape projected part is formed on 
each corresponding side surfaces. 
It is possible to use the hollow members having the sectional views of 
FIGs. 2(b) to (f) as well as FIG. 2(a), in combination as desired. It is 
preferable to form the quadrilaterial frame shown in FIG. 1 from the 
viewpoint of the strength of frame, the easy assemble, the maintenance of 
constant concentration in the electrolytic compartment. 
When the quadrilaterial frame is formed with four members, it is necessary 
to use at least two hollow members among four members. In the preparation 
of the rectangular frame, it is preferable to use the hollow members at 
least as the upper part and the lower part though the side parts can be 
only plate or block. 
The size of the frame is preferably in a range of 3 m to 0.2 m especially 2 
m to 0.5 m of height and 5 m to 0.2 m especially 3 m to 0.5 m of length. 
The ratio of the height to the length is in a range of 1/5 5/1 . The size 
of the hollow member is preferably 50 cm to 1 cm especially 20 cm to 3 cm 
of width in the section. The ratio of the width of the hollow member to 
the height of the frame is in a range of 1/5 to 1/100. 
In FIG. 3-1, one or more holes (7) are formed in the lower hollow member 
(3) so as to feed the solution into the electrolytic compartment. One or 
more holes (6) are formed in the upper hollow member (2) so as to 
discharge the solution from the electrolytic compartment. An inlet (8) is 
formed on the lower hollow member (3) so as to feed the liquid into the 
hollow member. An outlet (9) is formed on the upper hollow member (2) so 
as to discharge the solution from the hollow member. It is enough to form 
the upper and lower hollow members as the frame. 
However, as shown in FIG. 3-2, in order to decrease weight of the frame, it 
is preferable to form hollow members as the side parts (4) (5) of the 
frame. The hollow members as the side parts (4), (5) can be formed 
independently from the upper and lower hollow members without the 
communication. 
In said structure of the frame, the side parts (4), (5) of the frame are 
hollow members, it is possible to control the temperature of the 
electrolytic compartment by passing a heating medium or a cooling medium 
through the hollow members (4), (5). 
It is preferable to have the structure of FIG. 3--3, wherein the upper and 
lower parts (2), (3) and the side parts (4), (5) of the frame are formed 
by hollow members and the hollow member for the upper part is not 
communicated to the hollow members for the side parts and the hollow 
member for the lower part is communicated to the hollow members of the 
side parts, whereby the weight of the frame can be lowered and the 
apparatus can be compact for the circulation of the electrolyte described 
below. 
The material of the frame can be selected depending upon the type of the 
solution and the gas contacted. Typical materials include titanium, and 
the like for anolyte compartment, and iron, nickel, stainless steel and 
like for catholyte compartment. It is also possible to use the material of 
the frame coated with a fluorine type resin such as vinylidene fluoride 
polymers, tetrafluoroethylene polymers and tetrafluoroethylene-ethylene 
copolymers. 
As stated above, various structures of the frame can be formed by 
assembling the hollow members. 
In order to form the holes for feeding or discharging the solution and the 
gas, the holes are formed for communicating between the central opening 
and the hollow member on the inner surface of the hollow member. The work 
for forming the holes on the surface of hollow member is easily conducted 
by the conventional method. 
In the case of the electrolytic cell having the frames of the invention, as 
shown in FIGS. 4-1, 4-2 and 6, the frame for catholyte compartment (11) 
having the cathode (10), the gasket (12), the ion exchange membrane (13), 
the frame for anolyte compartment (15) having an anode (14) are arranged 
and the frames are fastened to form the electrolytic compartments of the 
catholyte compartment (16) and the anolyte compartment (17). The anode is 
preferably an insoluble electrode such as platinum group metal, a titanium 
coated with a platinum group metal and a titanium coated with a platinum 
group metal oxide. 
The cathode is preferably made of iron, stainless steel and nickel. The 
shape of the electrodes can be net shapes (gas generated by electrolysis 
is not remained), and plate shapes. The diaphragms are cation permeable 
membranes which have oxidation resistance and chlorine resistance and 
fluorine-containing polymer type cation-exchange membranes e.g. copolymer 
of tetrafluoroethylene and sulfonated perfluorovinyl ether; copolymer of 
tetrafluoroethylene and carboxylated perfluorovinyl ether and the like. 
The latter cation-exchange membranes are preferably used. 
In the case of the diaphragm type electrolytic cell using the 
cation-exchange membrane, it is possible to insert a spacer between the 
cation-exchange membrane and the electrode so as to prevent direct 
contact. The spacer can be chemical resistant material such as a net of 
polyolefin or florine-containing polymer. The ion-exchange membrane, the 
spacer and the electrode are held with a packing between the frames. 
The electrodes can be disposed in the frames by fixing each electrode 
leading holder on each frame and each electrode is held on the electrode 
leading holder. 
In the three compartment type electrolytic cell having an intermediate 
compartment between the anolyte and catholyte compartments, the frame for 
anolyte compartment having the anode, the diaphragm, the frame for 
intermediate compartment, the diaphragm and the frame for catholyte 
compartment having the cathode are arranged in series and are fastened to 
form the electrolytic cell. 
In the case of the monopolar type electrolytic cell, the anolyte 
compartments and the catholyte compartments are electrically connected in 
parallel for each electric polarity. 
In the feed of the current from the outer power source to the frame, a lead 
rod is electrically connected to electrodes having the same electric 
polarity. It is possible to hold the electrodes in the frame through the 
lead rod by mechanically fixing the lead rod to the electrodes. 
The case of monopolar type electrolytic cell has been illustrated. 
The bipolar type electrolytic cell can be formed by alternatively arranging 
the electrodes (one surface of the partition is cathode and the other 
surface is anode), the frames and the ion-exchange membranes and fastening 
them. The both frames and the partitions can be welded in one piece. 
In the bipolar type electrolytic cell, the frame/anode-cathode/frame is 
considered as one anode-cathode frame and the frames and the ion-exchange 
membranes are alternatively arranged and they are fastened. 
The anode-cathode frames are connected in series. 
In both of the monopolar type and bipolar type electrolytic cells, the 
upper parts of the frames are respectively connected to gas-liquid 
separators. 
In usually, the anolyte compartments are connected to one or more 
gas-liquid separator, and the catholyte compartments are connected to the 
other gas-liquid separator. When an aqueous solution of sodium chloride is 
electrolyzed, the anolyte compartments are connected to hydrogen gas 
separator and the catholyte compartments are connected to chline gas 
separator. These gas separators are disposed out side of frames. 
The flow of the solution in the electrolytic cell of FIGS. 4-1 and 4-2 for 
the electrolysis of an aqueous solution of sodium chloride will be 
illustrated referring to FIGS. 5-1, 5-2, 5-3 and 6. 
Firstly, the flow of the solution in the electrolytic cell using the frames 
shown in FIGS. 3-1 and 3-2 will be illustrated referring to FIGS. 5-1, 5-2 
and 6. 
FIGS. 5-1 and 5-2 are respectively sectional views of the electrolytic cell 
of FIG. 4-1 having the frames of FIGS. 3-1 and 3-2 taken along the line 
C--C. 
FIG. 5-1 shows the structure of the anolyte compartment and the flow of the 
solution in the compartment. 
The catholyte compartment is formed with the same type frames (not shown) 
as it is clear from FIG. 6 which is a sectional view taken along the line 
D--D in FIG. 4-1. 
The saturated aqueous solution of sodium chloride or the like is fed from 
the inlet (8) to the hollow zone (3) corresponding to the lower part of 
the frame (15) for the anolyte compartment (11) and it is passed through 
the holes of (7) to the anolyte compartment wherein in the electrolysis is 
conducted to generate Cl.sub.2 gas. 
The electrolyzed solution rises in the compartment by the gas-lift action 
with the gas and is passed through the holes (6) to the hollow zone (2) 
corresponding to the upper part of the frame of the anolyte compartment 
and the solution containing the gas is discharged through the outlet (9) 
to out of the frame. 
As the same time, in the frame for the catholyte compartment, water or a 
dilute aqueous solution of sodium hydroxide is fed from the inlet to the 
hollow zone corresponding to the lower part of the frame and is passed 
through the holes to the catholyte compartment, wherein the electrolysis 
is coducted to produce the aqueous solution of sodium hydroxide and to 
generate hydrogen gas. 
The electrolyzed solution rises in the compartment with the gas and is 
passed through the holes to the hollow zone corresponding to the upper 
part of the frame (11) and the solution containing the gas is discharged 
from the outlet. 
The gases discharged from the frames of the anolyte compartment and the 
frames of the catholyte compartments are respectively fed to the 
gas-liquid separators (18) wherein the gases are separated. Each part of 
the separated solutions is flowed down through the solution falling pipe 
(19) to the hollow members (3) in the lower parts of the frames and it is 
recycled into each of the anolyte compartments or the catholyte 
compartments. 
The gas-liquid separators can be connected to each of frames and they can 
be connected to a group of the frames of the same type compartments as the 
common separators. Thus, the concentration of the solution in the frames 
of the same type compartmemts can be uniform, whereby the condition of the 
electrolysis in whole of the compartments can be maintained in the optimum 
condition. 
In usual, the gas-liquid separators need enough capacity for forming the 
gas-liquid intersurface. 
In the electrolysis using the ion-exchange membranes and the electrolytes 
at 80.degree. to 120.degree. C., the phenomenon of formation of a foam 
layer on the surface of the solution in the gas-liquid separator is found. 
Accordingly, in our invention, the gas can be easily separated by feeding 
the electrolyzed solution containing the gas from the above position of 
the foam layer in the gas-liquid separator. The capacity of the separator 
for the foam layer of 5-300 mm from the surface of the solution is enough. 
The capacity of the separator for the foam layer of 20-200 mm from the 
surface of the solution is more preferable. When the electrolyzed solution 
is fed below the surface of the solution in the gas-liquid separator, the 
thickness of the foam layer is too thick, whereby the discharge of the gas 
is prevented and suitable gas separation can not be attained. In such 
case, if the foam layer is reduced, a large capacity of the gas-liquid 
separator is needed. This is not advantageous from the viewpoint of the 
apparatus. 
The position of the gas-liquid separator is the same level of the outlet 
(9) of the frame for the higher level. 
The sectional view of the separator is preferably quadrileral or 
rectangular shape. 
The flow of the solution and the gas in the electrolytic cell shown in FIG. 
4-2 using the frames shown in FIG. 3-3, is illustrated referring to FIG. 
5-3. In FIG. 5-3, the flow of the solution and the gas in the anolyte 
compartment is shown. In the catholyte compartment (not shown), the kinds 
of the electrode and the frames are different but the structure is the 
same with the anolyte compartment. 
The flow of the solution and the gas in the catholyte compartment is the 
same with that of the anolyte compartment. 
The saturated aqueous solution of sodium chloride or like is fed into the 
hollow zones (3) at the bottoms of the frames (11) of the anolyte 
compartments in parallel and it is fed through the holes (7) into the 
anolyte compartments wherein the electrolysis is carried out to generate 
Cl.sub.2 gas. The electrolyzed solution rises with the gas by the gas-lift 
action and it is fed through the holes (6) into the hollow zone (2) at the 
upper parts of the frames of the anolyte compartments. The solution 
containing the gas is fed from the outlet (9) to the gas-liquid separator 
(18) wherein the Cl.sub.2 gas is separated. A part of the separated 
solution is flowed down through the solution falling pipe and it is fed 
into the hollow zone (5) of the side parts of the frames. The solution is 
flowed down through the hollow zone corresponding to the side part of the 
frame and it is fed into the hollow zone (3) corresponding to the bottom 
of the frames. The solution is further recycled through the holes to the 
anolyte compartments, together with the fresh saturated aqueous solution 
of sodium chloride or like. 
At the same time, water is usually fed through the inlet into the hollow 
zone corresponding to the bottoms of the frames of the catholyte 
compartments, and it is fed through the holes (7) into the catholyte 
compartments wherein the electrolysis is carried out to form an aqueous 
solution of sodium hydroxide and to generate H.sub.2 gas. The electrolyzed 
solution rises with the gas by the gas-lift action and it is fed through 
the holes into the hollow zone corresponding to the upper parts of the 
frames of the catholyte compartments. The solution containing the gas is 
fed from the outlet into the gas-liquid separator wherein H.sub.2 gas is 
separated. A part of the separated solution is flowed down through the 
solution falling pipe and it is fed into the hollow zone corresponding to 
the side parts of the frames of the catholyte compartments and it is 
flowed down and is fed through the hollow zone corresponding to the bottom 
of the frames into the catholyte compartments together with the fresh 
water. 
In accordance with the present invention, the gas-liquid separation of the 
electrolyzed solution is carried out in the gas-liquid separator out side 
of the frames, whereby it is unnecessary to have large capacity for the 
hollow zone at the upper parts of the frames and the electrolytic cell can 
be compact. Moreover, the upper and lower parts of the frames and the 
hollow members for the side parts can be the hollow members having the 
same sectional size whereby the preparation of the frames can be easy. 
The hollow zones corresponding to the upper, lower and side parts of the 
frame are not respectively communicated whereby the gas in the hollow zone 
corresponding to the upper part is not flowed into the compartment. 
Thus, the side parts of the frame are formed by the hollow member and the 
hollow zone corresponding to one side part of the frame is communicated to 
the hollow zone corresponding to the lower part of the frame to form the 
circulation path of the electrolyte whereby the electrolytic cell can be 
compact. 
The sectional size of the hollow members at the side can be large whereby 
the pressure loss can be small and the rate of the circulation of the 
solution which does not contain the gas can be high. 
In the electrolytic compartments, the rate of the circulation of the 
electrolyte is high whereby the ratio of the gas in the solution can be 
small and the rise of the voltage in the electrolysis caused by the gas 
can be prevented.