DRUM ELECTROLYSIS

Abstract: Electrolysis of metal from an electrolyte inside a rotating cathode drum during use of an in the drum existing solid, freely movable insoluble particle material, provides that electrolyted metal does not deposit on the drum walls but on the present particulate material.

Description: DRUM ELECTROLYSIS. The present invention concerns a process for electrolysis wherein there is used a movable electrode in addition to one loose and freely moving solid medium present in the electrode, and a device for performing the process. It is previously known to perform electrolysis with movable cathodes , but with such electrolysis the astened material will grow on the electrodes (the cathodes) , and with time they will become useless unless the separated metal is removed, for instance manually or in a auto¬ matical mechanical manner. Thus there has previously been performed electrolysis with sylindrical rotating cathodes where the separated metal is adhering on the outside of the electrode, and intermittantly must be removed so that the electrode will not become useless. If the anode at such electrolysis is placed inside a rotatable, for instance cylindrical, cathode, it might be expected that the cathode gradually would grow solid and become useless from the deposited metal. It has, however, surprisingly bee found that this does not occur if there is present a freely movable, solid medium inside the cathode drum. Such a freely movable medium may inter alia comprise metal particles or -spheres of the same metal as in the electrolyte, or of another conducting or non-conducting or inert material. By rotating the cathode, the particles will thus "polish" the inner surface of the cat o e drum, and at the same time the distance between anode and the spheres will be less than between anode and cathode drum. By using such a process and device for electrolysis, sepa¬ rated material will be deposited on the inner medium (spheres) and not on the cathode surface. At the same time there will be mentioned "en passent" that the free, solid medium inside the cathode drum need not necessarily be round or sperical, but can have any shape which accomplishes the above mentioned effects, and which makes the metal deposit on the particle surface of the medium. It will also in this connection be mentioned that the medium inside the the rotating or otherwise movable, f.ex. shaking or vibrating, cathode, also may comprise other devices, f.ex. scrapes or knives, which accomplishes a similar effect as the above mentioned solid medium. By adding into the rotatable cathode an electrolyte, optionall containing free particles of solid medium, there may, by draining poor electrolyte from the opposite end of the cathode, be produced continuously metal particles or -silt without the cathode drum growing solid. This makes that it in addition becomes easy to remove possible harmful or interfering gas which has been produced during the electro¬ lysis, by equipping the disclosed electrolysis drum with an outlet or a fan for such gas, or for gas which it may be advisable or necessary to store. Examples of devices which are suited to performing the above disclosed electrolysis process will below be described by reference to the attatched figures, where: Fig. 1 shows a cathode drum with anode discs therein reaching down into the electrolyte. Fig. 2 shows a cathode drum as in fig. 1, but seen from the side and with marked roll bearings. Fig. 3 shows another embodiment of a drum cathode which iε shown in fig. 1, but where the anode comprises an anode tube with holes for adding and discharging electrolyte and gasses Fig. 4 shows an additional embodiment of a cathode drum, where the drum is placed obliquely for suitable sedimentatio of the particle material, and where the anode tube is sur¬ rounded by a non-conducting sheet for refining electrolysis. A suited device for performing the electrolysis according to the present invention is shown in fig. 1 and 2, wherein the rotating cathode drum 1 with electrically isolated end plates 2 is suspended on roll bearings 3. The penetrating anode comprises a conducting anode rod 4 with anode plates 5, optionally made of lead or some other siuted material, hanging down into the electrolyte. The anode rod is connect to a positive terminal of a not shown current source. The freely movable, particulate medium inside the rotatable end rotating cathode drum 1, is given by the reference number 7. The particle material does not have any direct contact with the anode plate 5. Inside the cathode drum 1 there exists an electrolyte 8, which electrolyte may be drained, optionall together with produced silt and/or waste material, through a drinage opening 10, where the elctrolyte which is drained at 10 is poor in the current cation which is being electro¬ lysed. Electrolyte for electrolysis, and possibly containing particulate solid medium, is supplied at 9, and the drum cathode 1 is connected to a negative terminal of a not shown current scource at 11, f.ex. inter a/lia through a sliding connection . The direction of rotation for the cathode drum is given by outer arrows i fig. 2, and the current movement of the particulate medium is given by inner arrows in fig. 2. Another possible embodiment of the device according to the invention, is where the side walls 2 are removed, and where the particulate material may migrate towards the open ends of the cathode drum 1, and from there be taken out during rotation or shaking/vibrating of the cathode drum. Another embodiment of the device according to the present invention is depicted in fig. 3, where each part is provided with the same reference numbers as in figs. 1 and 2, but where the anode does not encompass anode plates, but only a tube which is perforated, and where the electrolyte solution stands in direct contact with the tube 4. This embodiment makes it simple to remove produced gass by suction or blowing at 10. Yet another device for performing the process by electro- lysis according to the invention is given in fig. 4, wherein the anode tube 4 is perforated here as well, but where the middle anode section 16-17 is provided with a non¬ conducting cloth 18 and where this section 14 has separate supplying devices 13 and exit devices 15 for particulate material, silt and solutions. For persons skilled in electro¬ lysis it will be close and obvious that suc a device may be used for refining of metals or electrolysis where so- called red/ox-pairs are present, such as in f.ex. electro¬ lysis of Cu I-cloride solutions (Cupro-solutions) where Cu II chloride is produced at the anode and may be suctioned through the cloth and out into the device 15, separately from the exit device of the cathode chamber 10. Produced gas, depicted by bubbles in the figure, is taken out through the outlet 12. Each reference number refers as well to the corresponding elements in the other figures. The cathode drum shown in fig. 4, is in addition inclined to produce sedimentation of the particulate medium according to particle size, where the large particles collect in the lower part of the cathode drum, an may therefrom easily be removed. Below some trials for productions of metal will be described by using the process according to the invention. Experiment 1: The purpose for this experiment vas to determine the effect of the process according to the invention during production of metal, i.e. to determine whether metal did not deposit on the cathode walls but on the particulate material in the cathode drum only. The cathode drum (diameter = 20 cm, length = 100 cm, made of 316 L stainless steel) was filled with 4,00 kg Cu-spheres (so-called "prills with a diameter of 3 - 5 mm, and approx. 9 1 electrolyte. (Intervals within which the particular general trial parameters lie, are: H-SO. - 50-200 g/1, metal concen¬ tration - 5-60 g/1 in the inlet, temperature - 25-30 C up to 70-80°C, metal cations - Cu 2+ , Ni + , Zn + , current 2 density - 50-2000 A/m , rotation of the cathode drum - 1-20 rpm (corresponding to 1-20 cm/sek. periperally) , weight of solid medium - 1-10 kg (corresponding to 100- 1000 kg/m ) .) The anode comprised in this trial 19 lead anode plates with a mutual distance of 5 cm inside the cathode drum. The electrolysis device was mounted on rolls, and a variable motor rotated the drum with 17 rpm while the anode was stationary. The device was heated by help of heating cables placed around the drum (2 x 400 W) and received their energy via two sliding contacts of 220 V. A contact thermostate regulated the temperature with 5 C accuracy. The positive end of a rectifier was connected to the anode rod which protruded from openings in the end walls of the cathode drum. The negative pole was connected to a 5 mm lead plate which slided against teh rotating cylinder and was kept in place by a spring, somehting which gave good contact without tendencies to spark production. The system coud withstand 200 A. Elelctrolyte was supplied through the one end of the cathode drum, and drained from the other end. Current was supplied when the working temperature was reached while the drum rotated continously. 5 Continous repacement of the particulate medium was not performed in htis experiment, and the particles were allowed to grow. The experiment was done during 9k hours at only 25-28 C by using 60 A. This gave a current density of 2 240 A/m at a cell voltage of 2,8 V. 0 The results of the experiment are given in table 1. By these operating conditions there was produced 0,3 kg copper deposited on the copper spheres in the solid medium in the cathode drum only. The drum walls per se were com- 5 pletely clean for copper deposits. Table 1. Electrolyte u 2+ H-SO. supply Temp. 20 Supplied the cell 3,3 gg//i1 44 g/1 9,6 1/h - Drained C g/i 92 g/1 9,6 1/h 28°C During the experiment there was also produced hydrogen, but this was effectively removed by suction. The trial shows 25 that metal is deposited on the solid medium only. Experiment 2: The same prcedure as in experiment 1 was used, but with 30 increased temeperature and a supply to the cell of 32 g/1 copper and a drainage from the cell of 5 g/1 copper to determine whether the solid medium (the copper spheres, "prills") still were produced at increased copper concen¬ trations without deposits of copper on the drum walls at "- • 5 50°C. The results are given in table 2. At the trials, 2 the cell voltage = 2,4 V, Current density = 240 A/m , Duration = 37 hours, Current efficiency = 70%. There was produced 1,8 kg metal on the solid medium alone. Table 2: Electrolyte Cu 2+ H 2 S0 4 supply Temp. Supplied the cell 32,0 g/1 176 g/1 1,74 1/h - Drained 5-7 g/1 260- 1,41 1/h 50°C 270 g/1 Experiment 3: The same procedure as in experiment 1 was used, except that this experiment was a copy of a true electro extraction procedure for copper, where the feed electrolyte is approx. 60 g/1 Cu and the drainage is 30-40 g/1 Cu at 55-60°C. The operating conditions were: Cell voltage = 2,7 V, 2 Current density = 240 A/m , Duration = 18 hours, Current efficiency = 55% (on account of Fe 3+) . There was at the trial produced 0,70 kg copper deposited on the medium material (the copper spheres) alone. The operating con¬ ditions are given in table 3. The trial shows that the process according to the invention may be used under usual conditions for electro production of metal. Table 3. Electrolyte nCu 2+ Fe 3+ H 2 S0 4 supply Temp. Supplied the cell 58 g/1 2 g/1 64 g/1 1,5 1/h Drained 35 g/1 2 g/1 107 g/1 1,4 1/h 55-60°C Experiment 4 The same procedure as in experiment 1 was used, except that 2 the current density was increased to 800 A/m , while the temperature was kept to 55-60°C with a supply of 32 g/1 Cu. (The cell current = 200 A, no iron in the supplied material.) The operating conditions are given in table 4. There was produced 0,66 kg copper which was deposited on the copper medium in the drum alone. The trial was performed with 2 cceellll vvoollttaaggee == 33,,33 VV,, CCuurrrreenntt ddeennssity 800 A/m , duration = 4 hours, current efficiency = 70%. Table 4. 2+ Electrolyte Cu H 2 S0 4 supply Temp. Supplied the cell 32,4 g/1 80 g/1 5,2 1/h Drained 0,1-0,4 g/1 140 g/1 4,8 1/h 55-60°C In connection with experiment 4 it is of interest to observe that the minimum content of metal ions in the drainage is 0,1-0,4 g/1. This shows that the efficiency of the process and with the device according to the present invention, is strongly improved compared to previous technique in the field. Experiment 5: The same procedure as in experiment 1 was used, except that the quantity of copper spheres ("prills") waε increased from 4,00 kg to 8,00 kg, and the feed electrolyte from experiment 4 was doped with small quantities of antimony (Sb) and arsenic (As) to determine the selectivity of the deposition of copper against antimony and arsenic. The trial was performed with a cell voltage of 3,0-3,6 V, 2 current density = 800 A/m , duration = 3 hours, temperature = 60°C, feed velocity of solution = 3,3 1/h, current = 200 A. The trial conditions an -results are given in table 5. Experiment 5 shows as in experiment 4 that the drained solution contains very little metal ions, and that the selectivity for depositing copper against antimony and arsenic is very good. Table 5. Cu 2+ H 2 S0 4 Fe 2+ Sb As Supplied the cell 27,3 g/i 117711 gg//1 1,4 g/1 90 mg/1 8 mg/ Time 5 in drain 28,7 II 85 ' 8 30 11 II 20,7 II 85 1 8 60 11 II 9,7 II 186 " 85 ' 8 90 II II 3,6 II 85 ' 9 105 II 0,75 II 85 ' 9 120 II II 0,13 II 1,6 59 ' 7 135 II 0,13 203 " 34 4 In this connection it is interesting to observe that the present invention opens for possibilities for use over and above only electro production and electro refining of metal such as f.ex. inter alia purification of electrolytes. Experiment 6. The same procedure as in experiment 4 was used, except that the solid medium inside the cathode drum was changed from copper spheres ("prills") to small bits (5 x 5 x 10 mm) of stainless steel (316 L) , the same material that the drum was made of. The trial conditions are given in table 6. During the trial there was deposited on the steel bits a copper layer in a quantity of 0,36 kg simultaneously as there was produced copper dust in a quantity of 0,47 kg. There was neither in this experiment deposited any copper on the walls of the cathode drum. The trial was performed 2 with cell voltage = 3,9 V, current density = 800 A/m , duration = 5,1 hours, current efficiency = 70%. Table 6 Electrolyte Cu 2+ H 2 S0 4 supply Temp. Supplied the cell 32,4 g/1 145 g/1 5,5 1/h Drained 0,4-0,6 g/1 210 g/1 5,1 1/h 55-60°C The trial shiws that the medium in the cathode drum needs to be present, but may be of a different material than the metal which is to be separated. This prevnets all the same depositing of material on the drum walls. Experiment 7. The same procedure as in experiment 4 was used, except that the solid medium inside the cathode drum was replaced with ground rock (- 25 + 4 mm) . This was performed to determine whether an inert medium (not electrically conducting) would prevent deposit on the walls of the cathode drum. The trial conditions are given in table 7. At the trial there was deposited the main part (approx. 450 - 500 g Cu) on the inside of the drum walls, while there was found 0,10 g copper particles in the solid medium in the drum. The trial was performed with cell voltage = 5 - 6 V, current 2 density = 800 A/m , duration = 3,6 hours. able 7 - Electrolyte supply Temp. Supplied the cell 32,0 g/1 145 g/1 5,5 1/h Drained 1-3 g/1 206 g/1 5,0 1/h 60-70°C The above given experiments show that if the conditions are right (e.g. metal concentration, temperature, stirring, current density etc.) in the cathode, an electrically con¬ ducting medium alone inside the cathode drum will effectively prevent deposition of metal on the drum walls. If the conditions by the electrolysis however favours silt/particle deposition (e.g. generally low metal concentration, low temperature, high current density and reduced stirring) , the solid medium works as a mechanical grinder, and it makes no difference whether the medium is electrically conducting or not. It is preferred that the solid medium should be of the same character as the metal which is removed from the electrolyte. The process and device according to the invention can accordingly advantageously be used for purification purposes during use of low current density.

Claims: C l a i s 1. Process at electrolysis using a rotating drum cathode and at least one anode, c h a r a c t e r i z e d i n that it inside the roatable and rotating cathode drum is applied an electrolyte which is brought in contact with at least one anode placed inside the cathode and electrically isolated therefrom, and in that there at least initially is provided an under the electrolysis conditions insoluble ^.articulate material, whereon electrlyted metal is deposited inside the cathode. 2. Process according to claim 1, c h a r a c t e r - i z e d i n that the particulate, insoluble material is provided and removed continuously from the rotatable drum cathode. 3. Process according to claim l or 2, c h a r a c - t e r i z e d i n that the electrolyte is added and removed continuously from the rotatable drum cathode. 4. Process according to claim 1 - 3, c h a r a c ¬ t e r i z e d i n that there inside the cathode drum is rotated at least one under the electrolysis conditions insoluble material comprising a metal and/or a metal alloy, preferably a metal of the same kind as the from the electrolyte separated metal. 5. Process according to claim l or 2, c h a r a c t e r ¬ i z e d i n that there in the cathode drum is rotated at least one under the electrolysis conditions insoluble material comprising an electrically inert material. 6. Process according to claim 1 - 5, c h a r a c t e r ¬ i z e d i that possibly produced gass is removed during the electrolysis. 7. Device for performing the process according to claims 1 - 6, c h a r a c t e r i z e d i n that it comprises at least one drum cathode (1) which may be rotated about at least on axis and which is connected to at least on current source, which drum cathode in addition preferable comprises end walls (2) which may be electrically isolated, in which end walls there is provided a centrally placed orfice through which there is provided means for supporting at least one anode (4) which is electrically isolated from the drum cathode, and which device in addition preferably comprises supply and drainage means for electrolyte and/or particulate, under the electrolysis insoluble material (9,10) , and in which cathode drum there is preεent an electrolyte (8) . 8. Device according to claim 7, c h a r a c t e r i z e d i n that it in addition comprises means for removal of produced gass (12). 9. Device according to claims 7 - 8, c h a r a c t e r ¬ i z e d i n that the anode at least comprises one in the electrolyte placed anode plate. 10. Device according to claims 7 - 8, c h a r a c t e r ¬ i z e d i n that the anode comprises a cylinder which is perforated for removal of possibly produced gass. 11. Device according to claims 7 - 10, c h a r a c t e r - i z e d i n that the rotation axis of the cathode drum is inclined with respect to a horizontal plane.

Inventors: THOMASSEN THOMAS, THOMASSEN, THOMAS
Applicants: CHEMINVEST AS, CHEMINVEST A.S.
Application year: 1988
Main classification: C25C1
IPC codes: C25C1, C25C7