GRANULAR MATERIAL

Abstract: Granular material consisting of microporous, substantially hollow granules of lead powder, i.e. a powdered mixture of lead and lead oxides, which comprises 0.5-2.0% by weight of a binder, has a particle diameter of 40-500 //cm and a bulk density of 2.4-3.4 g/cm<s3>s, and a method for the production of this material according to which a suspension of lead powder, binder and water is heated to 100-150`C and thereafter is spray-dried to granules. These granules can be used as the active substance in an eletrode plate in a lead accumulator.

Description: Granular material The present invention relates to a granular material con¬ sisting of microporous, substantially hollow granules of lead powder, which is a powdered mixture of lead and lead oxides, a method for the -production of this granular material as well as the use thereof "as an active substance in an electrode plate in a lead accumulator. The lead accumulator despite its great weight and rather considerable self-discharge is still the type of accumulator of greatest importance and it is reasonable to presume it will stay this way even in a force-seeable future. Thus, it is essen¬ tial to try to improve its construction and its capacity. De¬ pending on the range of use .a ' distinction is made between storage batteries, tractionary batteries and stationary batte¬ ries. In a conventional lead accumulator the electrode plates are formed as lead grids, the spaces of which through lubrica¬ tion have been filled with lead powder. During the first charge, the formation, the PbO and Pb in the lead powder are oxidized to PbO- in the positive plate and PbO is reduced to Pb in the negative plate, whereafter the cell is ready to be used. The electrode plate can also be of a tubular type, which is the case especially in tractionary and stationary batteries whereby a considerably improved life time is achieved. A tubu¬ lar electrode plate consists of a conducting grid frame of lead connected to a number of parallel central conductors, which each is surrounded by an inert, perforated tube casing, being sealed at the bottom. Between the casing and the central con¬ ductors the active material is placed, which normally consists of a pulverous lead powder. The production of these tubular electrodes is involved with certain difficulties as the active material is very fine-grained. In order to achieve an accept¬ able filling with a dry powder the tubes must be vigorously shaken and special vibration devices must be used. Furthermore, this dry filling is directly unsuitable from an environmental point of view as the powder easily raises dust and due to its toxicity, thus, requires the personel to use protective clothing andbreathing protections. To avoid these problems the s.c. wet filling method has been introduced by which the lead powder is mixed with sul- phuriσ acid and water to a homogenous paste which is pressed into the tubes.. . However, this method renders varying results and throughout a * decrease of the capacity. Another disadvan¬ tage is high installation costs and a "sticky" work requirin an intensive supervision. Through the production of granules of the lead powder the tubular electrodes can be filled by pouring without rais ing dust and without vibration. The obtained electrode filli also becomes very homogenous, i.e. the structural difference in the packed material which easily result from filling with powder are avoided. Furthermore, a much too dense packing making the electrolyte flow difficult is avoided. Thus, for a long time, one has tried to obtain granules of lead powder which could be used as an active material in electrode plate Different additives have been tested for the production of granules with a sufficient strength. SE PS 224,815, for example, discloses a method to produce particles of active material with the desired filling qualities wherein the mate rial is wetted with a ' mixture of a sparingly volatile and a volatile substance and is thereafter pressed through a sieve. DE AS 1,013,273 also discloses a method to produce granules which method consists of adding 5-15% additive to the active material while stirring, heating the active material to 300 and sieving. In order to avoid deposits in the accumulator cell whic decreases its life time one has also tried to produce granu¬ les without the addition of a binder of any kind. DE OS 1,817,966 discloses a method for the production of a PbO gra nulate free from binders according to which the active mate¬ rial is mixed with water and granulated in a known way in a granulator and dried. It is also known to mix the active mat rial with sulphuric acid and water and thereafter produce granules by pressing the mass through a sieve. OMPI The granules produces by previously known methods, how¬ ever, have proven to be worthless for industrial use in lead accumulators, either due to a deficient resistance which makes handling and storage impossible or due to the fact that 5 they leave deposists in the electrolyte and on the electrode plates which decreases the performance and life time of the accumulator. The object with the present invention is to achieve a granular material of lead powder fulfilling the requirements 10 for resistance, size and quality, and which, when being used as an active substance in a lead accumulator, does not dete¬ riorate its capacity and life time. This is achieved by means of microporous, substantially hollow granules containing 0.5-2.0% by weight of a binder, with a particle diameter of •. 3 15 40-500 μm and with a bulk density of 2.4-3,4 g/cm . The granules according to the invention are easy to handle and do not raise dust. They are mostly hollow and have a micro- porous structure making acid diffusion and convection possible and a bulk density which can easily be adjusted to an optimum 20 value within the stated interval 2.4-3.4 g/cm . Furthermore, and quite surprisingly, they show-a life time which considers ably exceeds the life time of earlier known porous granules when used as an active material in electrodes. The highly po¬ rous electrodes earlierly produced have initially contained 25 a substance being soluble in sulphuric acid, which substance by the formation, when the basic material is transferred to the electroch-eήically.'activelead dioxide/ is being released which results in a hollow space. The hereby formed electrode skeleton has had a tendency to disintegrate after some hundred 30 cycles of charging and discharging. The granules according to the invention, however, are extremely strong and have proved to have a life time of more than 1500 cycles. This life time is of the same order as for conventional batteries. " 35 Another advantage with a granular material according to the invention in comparison with a ' standard lead powder it is its ca¬ pability of a greater internal expansion, which in turn contribut es to a longer life time of the tube casings of tubular elect- OMPI < rodes.Pb and PbO- in the surface layer on the granules form in the presence of sulphuric acid while discharging the cell more voluminous PbSO.. The lead powder forming the basic material for the pro- duction of the granules is a pulverous, homogenous mixture o lead oxide (PbO)> metallic lead (Pb) and optionally red lead oxide (Pb 3 0 4 ) . The binder in the granules according to the invention must not influence the cell function or the corrosion of me lie lead in the used amount of 0.5-2.0% by weight. Neither must the binder be too soluble in sulphuric acid. As an exam ple-of possible binders we can mention water glass, differen plastic emulsions and polysacharides. A preferred binder acc ing to the invention is polyvinyl alcohol, preferably a water soluble one. One should, of course, strive to keep the binder content as low as possible and a preferred range is 0.8-1.5% by weight. The granular material may well comprise granules of two different size fractions, partly with a particle diameter of 40-60 ym andpartly with a particle diameter of 110-150 μm. Hereby a better filling degree is achieved than with a unifo size of particles, as well as an increased porosity and pore distribution, which favours the electrolyte flow. The granular material ' according to the invention is pro duced by suspending lead powder in water and addition of a binder whereafter the lead powder is transferred into granu¬ les. The method is characterized'bythe binder being added in an amount of 0.5-2.0% by weight calculated on- the dry substa the suspension being heated to 100-150°C and thereafter spra dried into granules with a diameter of 40-500 ym by pressing through a nozzle under pressure into a drying chamber of an elevated temperature. The granulation of the suspension of lead powder and bi der in water can be performed in a conventional spray drying apparatus with a container for the suspension from where the starting material under pressure and via an atomizer is pump into a drying chamber, into the upper part of which drying OMPI air is led, preferably heated to a temperature of 260-320 C. The product is removed from the lower part of the drying chamber which also is provided with anoutlet for the now moist drying air which, there, has a considerably lower tem- perature, 130-150°C. By varying pressure, temperature and bin¬ der content the " size of the granules can be controlled in a desirable way. The granular material according to the invention can be used as an active substance in accumulator batteries, preferab- ly in the positive electrode plate, which thereby has proven to obtain an improved capacity, but also in the negative plate. The granules can be used instead of lead powder in different types of lead batteries, but are particularly suitable for application in tubular electrodes, the production of which thereby is considerably simplified. A preferred shape of a tubular electrode, which results in a lead battery with a considerably elevated performance, a.o. an energy density of 40-45 Wh/kg cell, has, apart from granulated lead powder as an active material, a special geomet- ry which favours the electrolyte flow. The tube casings sur¬ rounding the central conductors which are connected to the grid frame are formed with an elliptical cross section and are dia¬ gonal in relation to the grid frame in an angle of 25-50°, and contact each other merely along one line. The invention will be further illustrated by means of the following examples on the production of granulated lead powder. EXAMPLE I 100 kg fine-powdered lead powder consisting of 30% Vi ^ . and 70% of a mixture of 70% PbO and 30% Pb was suspended in water to a dry content of 75%. Thereto was added, as a binder 1.5 kg MoviolT-R / ) 4-88, a polyvinyl alcohol with a hydrolysis grade of 88% and a viscosity of 4 cP for a water solution of 4%. The suspension was transferred to a closed pressure chamber, wherein it was heated and circulated. When the temperature of the suspension was about 125°C the spray drying was initiated. Hereto a spray drying chamber with a diameter of 2.2 lindrical height of 1.95 and a conical bottom part with an outlet for the final product was used. Drying air, heated directly with propane gas to a temperature of 290 G, was led into the upper part of the chamber and the moist air, the te perature of which had fallen to 140°C, was led out of the chamber through an outlet at its lower part. The suspension in the heated chamber was pumped to an upward directed nozzl placed 2.75 m below the ceiling of the chamber and was spray under a nozzle pressure of 1.5 MPa. By the expansion in the chamber free falling almost globular granules of lead-lead o of essentially two different size fractions with an average meter of 50 ym (60%) and 130 ym (40%) , respectively, were fo ed. These granules were porous and had a bulk density of 3.2 g/cm . EXAMPLE II In accordance with Example I and by using the device de¬ scribed therein, 50 kg lead powder were suspended with 12.5 water and 1.5 kg sodium silicate of 30%. This suspension was dried at a chamber temperature of 260°C/150°C and a nozzle pressure of 0.8 MPa and gave free flowing granules with a bul 3 density of 2.40 g/cm and with a somewhat larger particle diameter than in the preceding example. A sieve analysis sho that 83% of the granules have a diameter larger than 120 μm a 42% a diameter larger than 177 μm. Granules produced in accordance with Example Iwithout a..b by heating lead powder in water and sulphuric acid and by con version of the suspension in an analogue way, were hard to dr were not free flowing and had a poor mechanical resistance. To determine the capacity and the overpotential, four cells were tested, of which three were test cells with granu¬ lar material produced in accordance with Example I and one wa a reference cell with conventional lead powder. Each cell com prised two dry charged plates of porous lead of the dimension 24 x 140 x 1.7 mm as negative electrodes and as a positive electrode elliptical tubes filled with an active material in an amount of 17.8 g, 18.3 g, 17.9 g (the test cells) and 18.2 g (the reference cell) , respectively. As an electrolyte 130 ml 3 H 2 S0 4 with the density of 1.28 g/cm was used, i.e. surplus acid. The cells were formed at 50 mA for four days, thereafter at 300 mA until-at least 300 % of the necessary amount of elec¬ tricity had been introduced. The potential progress was register¬ ed on a recorder with a reference electrode of a cadmiumtype "Tudor RCD" . No measurable difference in the potential between reference cell and test cells could be noted during the forma¬ tion. The discharge was performed with about 1 h current (= 0.6A) and with 1/4 h current (= 1.0A) , which means that the cells were heavily loaded. Furthermore, the cells were completely discharged from time to time, i.e. the positive electrode was kept for some time on a lower potential than the negative electrode. Despite this fact the cells all the time showed good capacity qualities after a renewed charging. The capacity of the cells appears from the following table illustrating the time of discharge in nine 0.6A dis¬ charges. TABLE 0.6A discharge Discharge lapse, min • No " . Reference cell Test cells 1-3 1 53 52 - 56 2 51 53 - 56.5 3 43 48.5 - 50.5 4 52.5 58 - 60 5 52 59.5 - 62.5 6 42.5 49.5 - 52 7 49 58 - 61 8 33 42 - 44.5 9 50.5 59 - 63.5 OMPI /j. WIPO - * The lower values for the discharges 3, 6 and 8 are due to the previous complete discharge as well as three 1.0A dis charges before 3, complete discharge and two l.A discharges before 6, and complete discharge before 8. Charges and dis- charges were made with a constant current and all the cells were put to work, following exactly the same pattern. The table clearly shows that the granule cells after th second discharge already have higher capacity values than th reference cell. Particularly high values are achieved for th granule cells after the complete discharges (3, 6, 8) which a good indication of the resistance of the test cells. Vario self-discharges during shorter and longer periods of time showed that the test cells did not have a higher self-discha than cells without polyvinyl alcohol. Furthermore, after abo 100 cycles, the test cells still showed a higher capacity th the reference cell. Measurements of the hydrogen overpotential of the negat electrodes showed that the hydrogen overpotential of the re¬ ference cell was somewhat higher than the one of the test ce This means that, when charging, hydrogen gas starts developp somewhat earlier in cells with polyvinyl alcohol in the elec lyte. The examined test cells, however, showed a good charg ing susceptibility and the zero passage when charging occurr at the same time as for the reference cell. In cells with p vinyl alcohol the surface absorption of hydrogen gas was als surprisingly reduced, probably due to the fact that the nega electrode becomes covered with a thin film of polyvinyl alco hol. This results in the disappearance of the hydrogen gas a the potential will quickly rise to the balance position. Life time tests were performed with tubular electrode plates of the size of a storage battery filled with granules produced in accordance with Example I. After 2 h discharging to 1.60 V and subsequent 5 h charging a life time of about 800 cycles was achieved. The capacity had then fallen to 85% of the original value. This means that tubular electrodes filled with granules according to the invention have the sam life time as tubular electrodes filled with a pulverous lead powder. ^ s ( OMPI The carried out experiments show that tubular electrodes with granules according to the invention render at least 10% and up to 30% higher capacity than tubular electrodes filled with the same amount of ordinary lead powder at a relatively high load. This is quite an important improvement, especially considering that the.polyvinyl alcohol which has been released from the granules contrary to expectation merely has a very insignificant influence on the chargability and life time of the cell, which stay of the same order as for conventional powder cells.

Claims: CLAIMS : 1. Granular material consisting of microporous, substa ly hollow granules of lead powder, which is a powdered mixtu of lead and lead oxides, c h a r a c t e r i z e d i n that the granules comprise 0.5-2.0% by weight of a binder, have a particle -diameter of 40-500 urn and a bulk density of 2.4-3.4 g/cm 3 . 2. Granular material according to claim 1, c h a r a t e r i z e d i n that the binder is a polyvinyl alcohol. 3. Granular material according to claim 1 or 2, c h a r a c t e r i z e d i n that the binder is present in an amount of 0.8-1.5% by weight. 4. Granular material according to anyone of the claims 1-3, c h a r a c t e r i z e d i n that the granules are present in substantially two fractions with a particle diame¬ ter of 40-60 jum and 110-150 urn, respeetively. . 5. Method for production of a granular material of lea powder according to anyone of the claims 1-4, wherein the lea powder is suspended in water and a binder is added whereupon said suspension is transferred into granules, c h a r a c t r i z e d i n that the binder is added in an amount of 0.5-2.0% by weight calculated on the dry substance, the sus¬ pension is heated to 100-150°C and thereafter spray-dried to granules with a diameter of 40-500 μm by forcing through a nozzle under pressure into a drying chamber of an elevated temperature. 6. Method according to claim 5, c h a r a c t e r i z i n that the binder is a polyvinyl alcohol and the tempera¬ ture of the drying air in the drying chamber varies from an inlet temperature of 260-320 C to an outlet temperature of 130-150°C. 7. Method according to claim 6, c h a r a c t e r i z i n that the suspension is heated to 125 C, is forced throu a nozzle under an overpressure of 1.5 MPa into a drying cham¬ ber wherein a drying air of a temperature of 290 C is led. OMPI WIPO 8. Use of granules of lead powder according to anyone of claims 1-7, as the active substance in an electrode plate in a lead accumulator. 9. Use according to claim 8, c h a r a c t e r i z e d i n that the electrode plate is a tubular electrode plate with a grid frame of lead connected to parallel central con¬ ductors, which each is surrounded by an inert, perforated tube casing, sealed at the bottom. 10. Use according to claim 8 or 9, c h a r a c t e ¬ r i z e d i that the electrode plate is shaped with elliptical tube casings being diagonal in an angle of 25-50° in relation to the grid frame and are in contact with each other merely along one line.

Inventors: LINDHOLM A, MAGNUSSON R
Applicants: LINDHOLM A
Application year: 1980
Main classification: B01J2
IPC codes: H01M4