This application is a 371 of PCT/2003/007542 filed Jul. 11, 2003.
The production of chlorine by electrolysis of solutions of alkali halides, particularly of sodium chloride solutions, is nowadays the electrochemical process by far of greatest industrial relevance: it can be carried out by means of three different technologies, namely membrane, diaphragm and mercury cathode electrolysis.
The first technology, which is the most advanced and most recently established, is characterised by lower energy consumption resulting from lower cell voltage and reduced use of steam required for caustic soda concentration. The two other techniques are negatively affected to a large extent by the substantially greater energy consumption due to the higher cell voltage and, in the case of diaphragm cells, to the considerable amount of steam required for concentrating caustic soda up to the commercial value of 50% by weight. However, despite the obvious advantage, the membrane technology is still characterised by a lower than expected market penetration, having only been used up to now for the construction of few new plants and the replacement of diaphragm and mercury cathode plants already obsolete and of hard maintenance. This situation is practically due to the fact that the existing diaphragm and mercury cathode plants have essentially no capital costs, since all of them were built in the seventies and eighties, later experiencing continuous improvements, which have essentially solved the problems of environmental pollution associated with the release of asbestos fibres and mercury, meanwhile improving their energetic consumption and thereby reducing their gap versus the membrane technology.
In the specific case of diaphragm plants, the diaphragms consisting of asbestos fibres bonded with perfluorinated polymers were overcome by the diaphragms consisting of perfluorinated polymer fibres hydrophilised by means of various additives, for example fibres or particles of zirconium oxide. Furthermore, the conventional expandable anodes made of titanium activated by platinum group metal oxides were substantially improved thanks to a so-called zero gap version, provided with devices capable of exerting an elastic pressure and bringing the anode movable surface in direct and extended contact with the diaphragm as described in U.S. Pat. No. 5,534,122; moreover said anodes have been equipped with double expanders, in other words connections allowing the passage of electric current from the movable surfaces of the anodes to the current distributing bars, with appreciable ohmic drop reduction, as illustrated in U.S. Pat. No. 5,993,620. Furthermore, the anodes can be advantageously provided with devices allowing a significant increase of the internal recirculation of brine with a consequent advantage in terms of lower voltage and decreased oxygen evolution, two factors both allowing to reduce the energy consumption per ton of produced chlorine: this latter improvement is described in U.S. Pat. No. 5,066,378. Finally, the replacement of the rubber linings used to protect the copper bases whereon the anodes are fixed with titanium sheets, and the use of new types of elastic seals between cathode body and anode supporting base and between each anode and its supporting base as indicated in WO 01/34878 have allowed to considerably extend the operating lifetime of the individual cells which constitute an electrolysis plant: this resulted in a further reduction of maintenance costs and a greater production capacity with unchanged cell design.
A very clear description of the operation of the chlor-alkali diaphragm cells is given in Ullmann's Encyclopedia of Chemical Technology, 5a Ed., Vol. A6, pp. 424-437, VCH, while details of the internal structure of these cells are exhaustively illustrated in the figures of U.S. Pat. No. 5,066,378.
As it can be noticed, the several proposals made in the years to improve the operation of the diaphragm cells are essentially directed to finding more or less drastic modifications of diaphragms and anodes with the relevant way of their fixing to the supporting base, whereas substantially poor attention was devoted to the cathodes, both as concerns the cathode body with the relevant electrical connections and the structure of the active cathodic surface whereon the hydrogen evolution reaction and the formation of caustic soda take place. In particular, the latter element, namely the active cathodic area, consists of a conductive surface provided with holes, such as a mesh of interwoven wires or a perforated sheet both made of conductive material, generally carbon steel, shaped as to form prism-like structures with rather flattened rectangular section fixed by welding to a perimetrical chamber, equally consisting of interwoven wires or of a perforated sheet, connected to the side walls of the cathodic body and provided with at least one nozzle on the bottom to provide an outlet for the solution containing the product caustic soda and the depleted sodium chloride, and with at least one nozzle on the top for the hydrogen discharge. On these structures, known to the experts in the field as “fingers”, the diaphragm is deposited by means of vacuum suction from an aqueous suspension containing the polymer fibres and particles which, as previously mentioned, constitute the diaphragm itself. In the diaphragm cell structure, the diaphragm-coated fingers are intercalated with the anodes and the surface thereof can either be in contact with that of the diaphragms or spaced therefrom by few millimeters. In both cases the fingers shall not undergo any flexure that would cause abrasions on the diaphragm with consequent deterioration thereof. Moreover, during operation the current must be transmitted as uniformly as possible to the entire surface of the fingers: a non uniform distribution would involve an increase in the cell voltage and a decrease in the efficiency of caustic soda generation with simultaneous higher oxygen content in chlorine. As a consequence, for the best result, the fingers must be provided with adequate stiffness and at the same time with high electric conduction.
According to U.S. Pat. No. 4,138,295 granted to Diamond Shamrock Technologies SA, Switzerland and to the more recent patent application WO 00/06798 filed by Eltech Systems Corp., USA, the fingers are provided with a longitudinally corrugated internal sheet made of carbon steel or copper: the mesh of interwoven wires or the perforated sheet is fixed, preferably by welding, to the vertices of the corrugations well solving the problems of the homogeneous current distribution and of the stiffness. However the corrugations, developed as mentioned in the longitudinal direction, do not allow the hydrogen bubbles to rise freely in the vertical direction, to subsequently gather along the upper generatrix of the fingers and enter therefrom the perimetrical chamber equipped as said with at least one outlet for the gases. The longitudinally corrugated sheet forces hydrogen to gather below each of the corrugations and to flow longitudinally along each corrugation until exiting through appropriate openings into the perimetrical chamber: since this flow can hardly be equalised, the amount of hydrogen present under each corrugation is variable and occludes to a different extent the corresponding facing zone of the diaphragm. Hence, it can be concluded that the longitudinally corrugated internal sheet causes an inevitable unbalance of the electric current distribution. This unbalance, in its turn, leads to an inhomogeneous concentration of the caustic soda with a negative impact on both the faradic efficiency and the oxygen content in chlorine.
Also U.S. Pat. No. 4,049,495 granted to O. De Nora Impianti Elettrochimici S.p.A, Italy, describes the use of corrugated internal sheets, but with vertically arranged corrugations: in this case it is obvious that hydrogen can freely gather in the upper portion of the fingers, but its flow towards the perimetrical chamber is hindered by the upper portion of the corrugations. Furthermore, for a given electric current distribution, the stiffening effect of the vertical corrugations may be unsatisfactory.
U.S. Pat. Nos. 3,988,220 and 3,910,827, both granted to PPG Industries Inc., USA, disclose designs for the element inside the fingers similar to those just considered, respectively horizontal strips of perforated sheet and longitudinal conductive bars provided with vertical strips of sheet welded thereto. Though undoubtedly ensuring an appropriate stiffness, the latter solution entails the problem of the difficult hydrogen release discussed in the case of U.S. Pat. No. 4,049,495. The design of U.S. Pat. No. 3,988,220, on the contrary, represents a satisfactory answer to the requirements of stiffness, homogeneous current distribution and free hydrogen discharge, but only by means of a complex structure, difficult to be made and therefore unacceptably expensive. Moreover the structure of U.S. Pat. No. 3,988,220 does not allow the upward movement of hydrogen bubbles to create an appropriate recirculation of the product caustic soda inside the fingers: as a consequence of this missed recirculation, pockets of caustic soda at higher concentration may be present, particularly in case of anomalies in the electric current distribution and of diaphragm porosity, with negative impacts on the faradic efficiency and the oxygen content in chlorine.
It is therefore an object of the present invention to provide a novel finger structure particularly suitable for chlor-alkali diaphragm electrolysis cells, characterised by substantial stiffness and uniformity of electric current distribution, and capable of overcoming the drawbacks of the structures of the prior art.
Under a first aspect the present invention consists of a finger structure for chlor-alkali diaphragm cells provided with high conductivity and capable of ensuring a substantial homogeneity of electric current distribution on the whole surface of the fingers.
Under a second aspect the structure of the present invention is characterised by the necessary stiffness to prevent flexures capable of inducing abrasions against the anodes of said chlor-alkali diaphragm cells and possibly of damaging the diaphragm deposited on said fingers.
Under a third aspect the structure of the present invention allows the free upward motion of the hydrogen bubbles and the free flow of hydrogen, separated along the upper generatrix of the fingers, in the longitudinal direction towards the perimetrical chamber of the cells.
Under a further aspect the structure of the present invention facilitates the internal natural recirculation of caustic soda, induced by the upward motion of the hydrogen bubbles, ensuring a substantially uniform concentration inside the fingers.
These and other consequent advantages will be made clearer by the following detailed description of the invention.
The present invention consists of a novel structure for fingers of diaphragm electrolytic cells, particularly useful for chlor-alkali diaphragm cells.
In a preferred embodiment, the novel finger structure comprises a hollow portion defining an internal volume in fluid communication with a perimetrical chamber, the hollow portion housing a current distributing reinforcing element comprising a sheet or multiplicity of sheets provided with projections.
The invention will be described making reference to chlor-alkali diaphragm electrolysis cells for the sake of simplicity, but it is understood that the structure of the present invention can be applied to all diaphragm cells equipped with fingers; the structure of the invention allows to simultaneously achieve:
This set of advantages is achieved according to a particularly preferred embodiment of the invention using at least one current distributing reinforcement sheet longitudinally inserted inside each finger, wherein said sheet is provided with projections on both sides.
As shown in
Although the realisation of the projections by plastic processing, for example by deformation of the sheet using a suitable tool in an appropriate press, is the particularly preferred manufacturing process, manufacturing methods based on welding or brazing of projections, separately obtained, onto the flat sheet can also be used, and it is understood that the structures thus obtained fall within the scope of the present invention. However it is clear to the experts of the field that these methods require a labour commitment which makes them intrinsically slow and definitely more expensive than the method of plastic processing.
Although in
A particularly preferred aspect of the present invention is the arrangement of the projections according to a quincuncial pattern or the like, wherein no completely flat vertical portions of sheet are present: as made clear by
As a comparison with the quincuncial arrangement of
With reference to
Since the welding of the interwoven wire meshes or the perforated sheets gives the assembly a greater stiffness than that of the sheet alone, it is also possible to use pressed sheets provided with projections wherein completely flat vertical sections are present, as schematically shown in
In a further embodiment, the sheet provided with projections on both sides may be replaced by a couple of mutually contacting sheets, each provided with projections on the surface opposite to the contact surface.
As
The sheet provided with projections according to the invention subdivides the internal volume of each finger into two portions and the thickness thereof is practically nearly half the thickness of the finger wherein the sheet is installed. The volume of each portion is only partially occupied by the sheet projections, and therefore the ascensional movement of the hydrogen bubbles can easily generate an effective natural recirculation of caustic soda therein. This recirculation, indicated by arrows in
Though not strictly necessary, openings, not shown in the figures, can be made in correspondence to the residual flat areas of the sheets provided with projections according to the present invention: these openings are directed to favour the mixing of the caustic soda present in the two portions of volume formed inside each finger by the sheet of the present invention.
In order to allow a comparative evaluation of the validity of what disclosed in the present invention, two cells of a line of diaphragm cells of a chlor-alkali industrial plant fed with a current of 100 kA have been modified. The cells of the concerned line were provided with a cathodic body comprising fingers consisting of carbon steel interwoven wire mesh housing a 6 mm thick sheet, longitudinally corrugated as described in U.S. Pat. No. 4,138,295 and WO 00/06798: two of these cells, whose cathodic body after some years of operation showed an already worn out finger mesh, were subjected to the necessary procedures of replacement in a service site with reconstruction of the fingers by means of the same type of interwoven wire mesh previously used, but with modification of the internal sheet that was replaced in one of the two cells, hereinafter defined as cell A, by a couple of sheets provided with projections according to the present invention, and in the other cell, hereinafter defined as cell B, by the strips of perforated sheet described in U.S. Pat. No. 3,988,220. In particular the sheets according to the invention had a thickness of 6 millimeters and were provided with projections similar to spherical caps with an arrangement according to the quincuncial pattern of
The strips of perforated sheet of the fingers of the cell B having thickness of 6 millimeters have been inserted into each finger in such a number as to obtain a section for the electric current passage similar to that of the couple of sheets according to the invention installed in each finger of the cell A. The openings, made on each strip on three rows, had a diameter of 8 millimeters.
No additional modification was made on the remaining parts of cells A and B, except for the obvious installation of a new set of sealing gaskets between cathodic body—anodic base, cathodic body—cover, nozzles—pipes, and a new diaphragm.
After a few weeks of operation considered necessary for the stabilisation of the different components and particularly of the diaphragms, cell voltage, faradic efficiency of caustic soda production and oxygen content in the product chlorine were determined with the following results:
The above description is not to be intended as limiting the invention, which can be practised according to different embodiments without departing from its scope, and whose domain is solely defined by the appended claims.
In the description and claims of the present application, the word “comprise” and variations thereof such as “comprising” and “comprises” are not intended to exclude the presence of other additional elements or components.
Number | Date | Country | Kind |
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MI2002A1538 | Jul 2002 | IT | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/EP03/07542 | 7/11/2003 | WO | 00 | 12/27/2004 |
Publishing Document | Publishing Date | Country | Kind |
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WO2004/007803 | 1/22/2004 | WO | A |
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Number | Date | Country | |
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20050236269 A1 | Oct 2005 | US |