Abstract:
A gas producing high pressure electrolysis tank in combination with a water tank and pressure control and recollection valve units is capable to fill and recollect electrolyte automatically in the process of gas production. The electrolysis tank has good heat dissipation effect and is divided into a plurality of densely spaced electrolysis cells so as to make the electrolysis efficiency and pressure high.

Description:
BACKGROUND OF THE INVENTION 
     The present invention relates to a high-pressure gas producing electrolysis tank for use in safe generation of gas for commercial purpose. 
     In general, conventional gas production equipments produce gases by way of electrolysis in which the chemicals in various kinds of electrolyte will be electrolyzed so as to produce pure gases separately that are collected at last via collection procedures. The crucial factors effecting the efficiency of an electrolytic process are the concentration of an electrolyte, the material of the electrode plates, temperature, pressure of its operation environment and the distance between the electrode plates and etc. Control of the concentrations of electrolytes, the material of electrode plates and temperature of its operation environment can be easily achieved. However, the problem of inadequancy of pressure in a positive electrode chamber or negative electrode chamber (even it takes place for only a moment) is not tackled with ease, resulting in an irreversible damage to the partition boards in the electrolysis tank and in final sabotage of the whole electrolysis equipment. 
     Moreover, the inadequancy of pressure in the electrolysis tank results in the generation of air bubbles among electrode plates in a gas producing electrolytic process. The air bubbles will increase the electric resistance in the electrolysis, making the efficiency thereof decrease greatly. It becomes a common rule that the more air bubbles exist, the less efficient an electrolytic process becomes. If the bulk phase of an electrolysis has an electric resistance coefficient ρθ, and the bubble distribution layer has an electric resistance coefficient of ρ, and the resistance amplifying factor is f equal to ρ/ρθ. The maximum value of f can reach 6 in case of the bubbles being distributed in a rotary ellipse-shaped area. If the bubbles scattered in a bubble distribution area has a volumetric ratio (vacancy ratio), then the relation between the above factors is established as follows: f=ρ/ρθ=(1-ε) -1 .5. 
     Furthermore, if the distance between two electrode plates is excessively large, the electric voltage for the electrolytic process must be increased accordingly in such a manner that the loss of electrolytic effect will boost up at the same time. The conventional electrode plates are secured in place by metallic rods leading therethrough (space must be taken into account in assembly), resulting in a bulky size of the electrolysis tank. 
     To acquire a sound efficiency in an electrolytic process, the pressure in an electrolysis tank, the distance between two electrode plates must be properly controlled. But, it is quite difficult to achieve the goal by conventional techniques. 
     SUMMARY OF THE INVENTION 
     The primary object of the present invention is to provide a high pressure gas producing electrolysis tank in combination to a pressure control and recollection valve means so as to recycle electrolyte effectively. 
     Another object of the present invention is to provide a high pressure gas producing electrolysis tank having two mounting plates which are provided with a plurality of retaining ditches thereon for securing a plurality of partition diaphragms in place for dividing the degasing chambers of the electrolysis tank in a more effective manner so as to keep the operation pressure in the tank under proper level in spite of the high pressure generated in the tank resulting from reducing of the size of the tank and raising electrolytic efficiency. 
     The present invention has the following advantages given as below: 
     1. The pressure control and recollection valve means can condense the vapor in the produced gas and recollect electrolyte which can be recycled and automatically fed into the electrolysis tank so as to simplify the operation thereof; 
     2. The electrode plates are separated and secured in place by the retaining ditches on the two mounting plates so that the distance between two electrode plates can be minimized, making the assembly simple in one aspect and permitting a small volumed electrolysis tank to produce the same effect as in a large tank in another aspect (the present invention can accommodate 50 electrode plates in a 68-centimeter tank). Thus, the size of an electrolysis tank can be tremendously reduced and the efficiency of an electrolysis can be raised, permitting electrolyte to produce gas under high pressure without generating bubbles in operation. 
     3. The present invention can easily effect control of the pressure in an electrolysis tank and the distance between electrode plates and the fixing of the plates. 
    
    
     BRIEF DESCRIPTION OF THE DRAWINGS 
     FIG. 1 is a perspective diagram showing the exploded components of the present invention; 
     FIG. 2 is a diagram showing a practical application of the present invention; 
     FIG. 3 is a partially sectional view of the present invention; 
     FIGS. 4A, 4B are sectional diagrams showing the structure of the present invention; 
     FIG. 5 is a block diagram showing the flow chart of the present invention; 
     FIG. 6 illustrates the detailed structure of one of two mounting boards; 
     FIG. 6A is an enlarged view of circled area 6A in FIG. 6. 
     FIG. 7 is a plane sectional view showing the detailed structure of another embodiment of the present invention; 
     FIG. 8 is a diagram showing the structure of a separating board of the present invention; 
     FIG. 9 is a perspective diagram showing the exploded components of a third embodiment of the present invention; 
     FIG. 10 is an assembly of the third embodiment; 
     FIG. 11 is a diagram showing the operation mode of the separating board; 
     FIG. 11A is an enlarged view of circled area 11A in FIG. 11. 
     FIG. 12 is a diagram showing another design of the separating board; 
     FIGS. 13A, 13B, are diagrams showing one further embodiment of the present invention; 
     FIG. 13C is an enlarged view of circled area of 13C in FIG. 13A. 
    
    
     DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT 
     Referring to FIG. 1, the present invention is a high pressure gas producing electrolysis tank mainly comprising a top cover 1, a hood bracket 2, a pair of mounting plates 3, a pressure control and recollection valve units 4, a plurality of electrode plates 5, a plurality of partition diaphragms 6, a tank embodiment 7, a filter layer 8 and a water container 9. 
     The top cover 1 of a rectangular shape has a plurality of screw holes 11 disposed on two pairs of parallel edges and the axial middle line 10 thereof. The outlet disposed on each side of the axial middle line 10 for mounting of a check valve 12 respectively. 
     The hood bracket 2 has a left and right degasing chamber 21, 22 on the top portion thereof that are not in communication with each other. The hood bracket 2 has a plurality of downwardly protruded ribs 23 forming a plurality of receiving grooves among one another. It further has a plurality of spaced screw holes 25 disposed all over a peripheral flange thereof and a central division column 20 having a plurality of screw holes disposed thereon that correspond to the screw holes 11 on the top cover 1. The left and right degasing chambers 21, 22 have a plurality of degasing slots 211, 221 defined at each bottom face thereof respectively. The peripheral flange forming a surrounding wall 26 enclosing the downwardly protruded ribs and receiving grooves. At each short side of the left and right degasing chambers 21, 22 are disposed a plurality of recycling holes 27. 
     The degasing slots 211, or 221 are placed in correspondence to every other of the receiving grooves 28, as shown in FIGS. 4A, 4B. A plurality of electrode plates 5 each symmetrically folded into a clip form for saving material. 
     A plurality of partition diaphragms 6 each disposed under the protruded ribs 23 and consecutively next to electrode plates 5 alternatively in assembly with the top of the electrode plates 5 housed in the receiving grooves 28 of the hood bracket 2 and the partition diaphragms 6 located just under the downwardly protruded ribs 23 in an end-to-end abument relation. 
     A pair of mounting plates 3 each having a plurality of spaced vertical ribs 31 with a plurality of corresponding retaining ditches 32 forming among the vertical ribs 31 for mixedly housing the electrode plates 5 and the partition diaphragms 6 alternatively. A plurality of horizontal through holes 33 each bridging a pair of neighboring vertical ribs 31. Each mounting plate 3 is placed at one side of the electrolysis tank 7. 
     The electrolysis tank 7 is a container and has a plurality of heat dissipating fins 71 on external walls thereof and has a plurality of screw holes 72 disposed on the peripheral edge of the tank 7. The tank 7 has an electrolyte passing hole (not shown) on one side thereof and a level controller 75 (not shown) disposed near the top of one side wall with an electro-magnetic valve (not shown) and a pressure reducing valve (not shown) at the bottom of the same side. 
     A filter layer 8 including a pair of filter blocks 80 made of porous material each disposed on top of each the left and right degasing chambers 21, 22 respectively are retained in place by strips of weight block 81. 
     Pressure control and recollection valve units 4 each having a filter container 41 to the top of which are mounted a pressure control valve 42, a pressure relief valve 46, a pressure operated switch 47, a pressure gauge 48, explosion-proof outlet 45. At the bottom thereof is further disposed a check valve controlled gas inlet 44 and an electromagnetic valve 43 connected to the water tank 9. The pressure operated switch 47 automatically cuts off the general electric power supply as a pressure differential is applied thereto. 
     The water tank 9 containing an electrolyte therein is disposed between the electrolysis tank 7 and the pressure control and recollection valve units 4 and is provided with a level control means 91 inside thereof for regulating the level of the electrolyte therein. An electromagnetic valve 43 is disposed at the outlet of the tank 9. As the level control means 91 detects inadequacy of electrolyte in the tank 9, the general power supply is cut off at once. 
     In assembly, the mounting plates 3 are first secured in place to the right and left inner sides of the electrolysis tank 7 respectively with the retaining ditches 32 of the two mounting plates 3 in face-to-face alignment with each other, then the electrode plates 5 and the partition diaphragms 6 are placed in the retaining ditches 32 alternately in parallel to one another. To the bottom of each symmetrically folded electrode plate 5 are attached cushion members 76 so as to create a closed area. 
     Next, the hood bracket 2 with its flanged surrounding wall 26 is topped over the opening of the electrolysis tank 7 with the downwardly protruded ribs 23 of the hood bracket 2 in connection to the partition diaphragms respectively so as to form a plurality of cells 73 for housing the electrode plates separately. The top of each electrode plate 5 extends over the bottom edge of the protruded ribs 23. The top level of electrolyte is over the top of the electrode plate 5 and is under the right and left degasing chambers 21, 22. The arrangement of the degasing slots 211 of the degasing chamber 21 and the degasing slots 221 of the degasing chamber 22 is such that the slots 211 and the slots 221 are alternately positioned with one another, as shown in FIG. 4A, 4B. In other words, each slot 211 and slot 221 alternately come in registration with a different electrode plate 5. 
     A set of electrode plates 5 in registration with the degasing slots 211 of the left degasing chamber 21 are electrically coupled in parllel in the same manner as the other set of electrode plates 5 in registration with the degasing slots 221 of the right degasing chamber 22 by way of coupling wires 77 specially processed to keep it insulated and corrosion-proof and led through the filter layers 8 to extend into the degasing chambers 21, 22 respectively. Then, the top cover 1 is secured to the hood bracket 2 by way of screws 74 led through the screw holes 11 of the top cover 1 and the screw holes 25 of the hood bracket 2 and the screw holes 72 of the electrolysis tank 7. The water tank 9 is connected to the pressure control and recollection valve units 4 by tubes 40a one end of which is coupled to the electromagnetic valve 43 of the unit 4 and the other end coupled to the water tank 9. The check valves 12 of the electrolysis tank 7 are connected to the inlets 44 of the units 4 by way of tubes 40b, as shown in FIGS. 2, 3. 
     In practical operation, as the electrode plates 5 coupled in parallel by wires 77 led through the degasing slots 211, 221, are supplied with electrical power, the electrolyte, such as NaCl, there is an electrolysis cell 73 formed between each pair of electrode plate 5 as a result of the parallel connection of the plates. The positive electrode plates 5 will attract the negative ions in the electrolyzed solution to generate chlorine gas and the negative electrode plates 5 will produce hydrogen gas (forming NaOH solution due to the partition diaphragms). The produced gases confined in respective cells 73 formed by the diaphragms 6 and the protruded ribs 23 will be led into the left degasing chamber 21 via the slots 211 and into the right degasing chamber 22 via the slots 221 respectively. 
     The protruded ribs 23 stick into the electrolyte so that the space above the electrolyte and the ribs 23 can accommodate relatively high pressure electrolytic gases therein. At this moment, the filter layer 8 will remove moisture in the gases passing therethrough first time, and the moisture will be condensed into electrolyte again and be recollected via the degasing slots 211, 221 and the recycling holes 27 into the electrolysis cells 73. 
     The gases filtered by the filter layer 8 led through the check valves 12 and into the pressure control and recollection valve units 4 are filtered the second time in the filter tanks 41 so that gases with moisture can be finely filtered to produce dry gases and released via the pressure controlled valves 42 for collection. The condensed moisture will be collected in the filter tanks 41 in the form of electrolyte. 
     As the level of the electrolyte in the tank 7 is checked by a level controller 75 to be inadequate, the electromagnetic valves 43 of the filter tanks 41 and the water tank 9 will be opened to let the electrolyte in the filter tank 41 flow into the tank 9 and the electrolyte in the tank 9 flow further into the electrolysis tank 7 automatically to fill the same to a fixed level. Since the filter ta. 
     As the level of the electrolyte in the tank 7 is checked by a level controller 75 to be inadequate, the electromagnetic valves 43 of the filter tanks 41 and the water tank 9 will be opened to let the electrolyte in the filler tank 41 flow into the tank 9 and the electrolyte in the tank 9 flow further into the electrolysis tank 7 automatically to fill the same to a fixed level. Since the filter taof electrolysis cells 73 so as to effectively reduce the volume of the tank 7 and increase the electrolytic areas of the electrode plates 5. As a result of fast electrolytic reaction taking place in the cells 73 of the tank 7, a high pressure will be constantly maintained in the tank 7, effectively preventing bubbles produced therein. The heat produced in the electrolytic process can be dissipated via the through holes 33 of the mounting plates 3 and the wall of the electrolysis tank 7 directly. The electrolyte in the cells 73 is confined in the room of the vertical ribs 31 and the inner wall of the electrolysis tank 7, as shown in FIGS. 6, 6A. 
     Moreover, in another embodiment of the present invention, when the electrode plates 5 of the present invention are serially connected, the hood bracket 2 is additionally provided with a plurality of retaining ribs 24 disposed between every two protruded ribs 23 so as to make the left degasing slots 211 and the right degasing slots 221 and the protruded ribs 23 and the retaining ribs 24 to form consecutive spaces. After the hood bracket 2 is secured to the electrolysis tank 7, the bottom of the retaining ribs 24 abut against the tops of the electrode plates 5 respectively so that the electrolyzed gases in the positive electrode plates 5 and the negative electrode plates can be released via the degasing slots 211, 221 and the pressure control and recollection valve units 4 and the electrolyte is recollected as shown in FIG. 7. 
     However, when electrolyte is filled into the electrolysis tank 7 undergoing electrolysis in the parallel form by way of the water container 9, in order to effectively control the electrolytic pressure in the individual electrolysis cells 73 for protection of the partition diaphragms 6 from damage, the structure of the hood bracket 2 is used in this case. Referring to FIGS. 8, 9, a separating board 92 having a E-shaped cross section and a plurality of parallel grooves 95 is provided with a pair of separated passages 93 on the underside thereof and the slots 94 above the two passages 93 are arranged alternatively between the parallel grooves 95 which are used to receive the bottom ends of the partition diaphragms 6. 
     Furthermore, on the right and left portion of both sides of the electrolysis tank 7 are disposed separately a refilling tube 96 and a recollection tube 97. The refilling tube 96 on one side of tank 7 corresponds to the recollection tube 97 on the opposite side of the tank 7 so that two water containers 9 are connected to the refilling tubes 96 separately; and and the supplementary electrolyte can be directed from the two water containers 9 to the electrolysis tank and distributed via the plurality of slots 94 and into the passages 93, as shown in FIG. 10, effecting a fast mixing and diffusion of the electrolyte. Moreover, the electrolyte in the electrolysis cells 73 can be discharged separately via the recollection tubes 97, as shown in FIGS. 13A, 13B, 13C. 
     Furthermore, when the separating board 92 is applied to a serially-arranged electrolysis tank, the slots 94 and the grooves 95 on the separating board 92 must be rearranged in a manner as illustrated in FIG. 12 wherein there are a combination of paired grooves 95 and a single groove 95 disposed in order on the separating board 92 with a single groove 95 located between every two paired grooves 95. And a slot 94 is placed to the right and left side of every single groove 95 at one end of the groove 95 alternatively, and so on so further. Thus, the electrode plates 5 (no cushion member 76 is used in this case) and the partition diaphragms 6 are located alternatively, rendering the electrolysis cells 73 in a non-communicating manner, as shown in FIGS. 13A, 13B, 13C.