Gravita Wins India SME 100 Award 2012

India SME 100 AwardGRAVITA INDIA LIMITED has been awarded as “India SME 100 Awards” in an Award Ceremony organized by Reliance Commercial Finance and Supported by Ministry of Micro, Small and Medium Enterprises (MSME). The Award was received by Mr. Rajat Agrawal, Managing Director of the Company. Total 42623 Nominations were received and 100 Best SME’s were selected based on evaluation process audited by SDRC.

The Awardees had interaction with Mrs. Vijayalakshmi R. Iyer, Chairperson and Managing Director of Bank of India, V. Balasubramaniam, Chief Business officer BSE Ltd., Mr. Parag Patki CEO of SMERA.

Gravita is planning for exceptional growth and towards this end it has upgraded and done expansion at its Jaipur manufacturing plant during the financial year 2012-13. Going forward, the Company is planning to enter into value-added products of Lead metal to cater to global requirements.

How Lead Acid Battery Works ?

Let me give you the big picture first for those who aren’t very detail oriented. Basically, when a battery is being discharged, the sulfuric acid in the electrolyte is being depleted so that the electrolyte more closely resembles water. At the same time, sulfate from the acid is coating the plates and reducing the surface area over which the chemical reaction can take place. Charging reverses the process, driving the sulfate back into the acid. That’s it in a nutshell, but read on for a better understanding. If you’ve already run from the room screaming and pulling your hair, don’t worry.

Lead Acid Battery

The electrolyte (sulfuric acid and water) contains charged ions of sulfate and hydrogen. The sulfate ions are negatively charged, and the hydrogen ions have a positive charge. Here’s what happens when you turn on a load (headlight, starter, etc). The sulfate ions move to the negative plates and give up their negative charge. The remaining sulfate combines with the active material on the plates to form lead sulfate. This reduces the strength of the electrolyte, and the sulfate on the plates acts as an electrical insulator. The excess electrons flow out the negative side of the battery, through the electrical device, and back to the positive side of the battery. At the positive battery terminal, the electrons rush back in and are accepted by the positive plates. The oxygen in the active material (lead dioxide) reacts with the hydrogen ions to form water, and the lead reacts with the sulfuric acid to form lead sulfate.

The ions moving around in the electrolyte are what create the current flow, but as the cell becomes discharged, the number of ions in the electrolyte decreases and the area of active material available to accept them also decreases because it’s becoming coated with sulfate. Remember, the chemical reaction takes place in the pores on the active material that’s bonded to the plates.

Many of you may have noticed that a battery used to crank a bike that just won’t start will quickly reach the point that it won’t even turn the engine over. However, if that battery is left to rest for a while, it seems to come back to life. On the other hand, if you leave the switch in the “park” position overnight (only a couple of small lamps are lit), the battery will be totally useless in the morning, and no amount of rest will cause it to recover. Why is this? Since the current is produced by the chemical reaction at the surface of the plates, a heavy current flow will quickly reduce the electrolyte on the surface of the plates to water. The voltage and current will be reduced to a level insufficient to operate the starter. It takes time for more acid to diffuse through the electrolyte and get to the plates’ surface. A short rest period accomplishes this. The acid isn’t depleted as quickly when the current flow is small (like to power a tail light bulb), and the diffusion rate is sufficient to maintain the voltage and current. That’s good, but when the voltage does eventually drop off, there’s no more acid hiding in the outer reaches of the cell to migrate over to the plates. The electrolyte is mostly water, and the plates are covered with an insulating layer of lead sulfate. Charging is now required.

Global supply of refined lead metal exceeded demand – ILZSG

Refined LeadThe International Lead and Zinc Study Group released preliminary data for world lead supply and demand during 2012. The data compiled by the ILZSG indicate that in 2012 global supply of refined lead metal exceeded demand by 64 kilo tonne. Over the same period inventories reported by theLondon Metal Exchange Shanghai Future Exchange and producers and consumers increased by 23 kilo tonne totalling 628 kilo tonne the year end.

Global lead mine production increased by 11.5% compared to 2011. Output was higher in a number of countries including Mexico, Peru, the Russian Federation and Turkey, however the increase was principally due to a reported 20.4% rise in China.Other key results are:

Rises in output of refined lead metal in the India, the Republic of Korea, the United Kingdom and the United States were largely balanced by reductions in Australia, Kazakhstan, Morocco, New Zealand and Spain resulting in a limited global increase of 0.2%. Output in China was at the same level as in 2011.

Despite a further decline in European demand for refined lead metal of 2.4%, world usage increased by 1.3%. This was primarily a consequence of higher demand in India, Japan, Mexico and the United States. Apparent demand in China was unchanged from 2011. China’s imports of lead contained in lead concentrates rose by 26.3% to reach a record of just over a million tonnes.

Cash Settlement and Forward Three Month Prices on the LME averaged USD 2061 and USD 2073 respectively during 2012, 14% and 13.3% lower than during 2011. The highest Cash Settlement Price of USD 2340 was recorded on 31 December and the lowest of USD 1744 on 27 June.

Source: ILZSG

Gravita Reports 146% increase in its Q3 Net Profits

Lead and Lead Alloys ManufacturerGravita India Limited, Jaipur, has announced its Financial results for the quarter ended December 31, 2012. Consolidated Net total income for the quarter was Rs. 11307.01 Lacs, showing an increase of 59% over the total income for the corresponding quarter of previous year.

The EBITDA of the Company increased by 189% in Q3 FY 2012-13 compared to the corresponding quarter of previous year. Over the last 10 months, the Share of the Company has gained 21% outpacing the Sensex’s 14.5% gain. In addition to above the Board of Directors of the Company have declared 2nd Interim Dividend for the Financial Year 2012-13 @15% on total issued capital of the Company.

The Company has recently expanded its Plant operations at Jammu and Senegal by implementing upgraded Plant & Machinery. The Company is in the process of establishing a new plant in Gujarat. The Company’s Jaipur Plant is also under expansion of production capacity. See Results on Gravita India Ltd.

Company Profile:

Gravita India Ltd. is Leading Indian Company having state-of-the-art Lead Processing unit at Jaipur (Rajasthan), INDIA. We carry out smelting of Lead Ore / Lead Concentrate / Lead Battery Scrap to produce primary & secondary Lead Metal, which is further transformed into Pure Lead, Specific Lead Alloy, Lead Oxides (Lead Sub-Oxide, Red Lead, and Litharge) and Lead Products like Lead Sheets, Lead Pipes etc. with proven technology and processes.

Casting Technology for Lead-Calcium Grids

Trends in grid design

In the U.S.A., automotive lead acid batteries using lead-calcium grids have dominated both the original equipment (OE) and the replacement markets in recent years. Over 90% of OE batteries are all-calcium, that is, both the positive and negative grids are constructed from calcium. This figure has increased from only 10% in 1975. A similar dramatic increase in the shift towards calcium grids has also occurred in the replacement sector. In 1975, less than 5% of replacement batteries used a calcium grids, today the share is 85% with 245 being all-calcium and 61% being a hybrid design (i.e., lead-antimony positive, lead-calcium negative).

Casting lead-calcium grids

Lead Calcium GridsCalcium alloys used in automotive lead acid batteries consist of a corroding grade of lead, about 0.08 wt% calcium, from 0.25 to 1.0 wt% tin, and perhaps some aluminium. From a casting standpoint, there are three major differences when comparing a calcium alloy with an antimony alloy containing between 2.75 and 5 wt% antimony. These differences are: (i) hardness after casting; (ii) oxidation rates at high temperatures; (iii) melting and solidification temperatures.

First, consider the problem of hardness after casting. The major differences between these two alloys is the hardness, or stiffness, of the grid immediately after ejection from the mould. The calcium alloy is much softer than antimony alloys at this stage and therefore it requires more careful handling by the casting machine and by the operator when removing and stacking the trimmed grids.

The second major difference is the respective rate of oxidation of the two types of alloy. The calcium alloy oxidizes, or drosses, more rapidly than antimony alloy. This makes calcium alloys more sensitive to agitation caused by lead pumps, the loading of pigs or scrap lead into the pot, or excessive lead temperatures.

The third difficulty lies in the melting and solidification temperatures. A common 4.5 wt% lead-antimony alloy is fully liquid at approximately 296ºC. When cooled down, it will start to solidify at 296ºC but does not become fully solid until it is cooled to about 252ºC. in the casting operation, this alloy must be poured into the mould and kept above 296ºC until the cast is complete. It must then be cooled about 26ºC before the grid can be ejected from the mould. By comparison, the calcium alloy is liquid at 327ºC. When cooled; it is solid at about 324ºC depending on the exact alloy composition. In the casting operation, this alloy must be poured into the mould and kept above 327ºC until the cast is complete, then cooled about 3ºC for the grid to solidify before being ejected from the mould. Thus, in a given example, the calcium alloy is liquid at approximately 25ºC higher than the antimony alloy and solidifies at a temperature that is approximately 54ºC higher. Therefore, to cast this alloy, it must be poured at a higher temperature and the mould temperature must be higher to prevent solidification before the cast is complete. In other words, calcium alloy runs hotter, it drosses more rapidly, and it is softer and more difficult to handle.

In more specific terms, differences in the operating temperatures of the two types of alloy are as follows.

  1.  Lead pot. Calcium is run slightly hotter (up to 10ºC) than 4.5 wt% antimony. Low antimony is even hotter at 454 C, and calcium-aluminium runs at 482ºC OR ABOVE.
  2.  Feedlines. These are operated at about 10ºC hotter for low antimony, calcium, and calcium-aluminium than for 4.5 wt% antimony.
  3. Ladle. Temperatures for calcium alloy are about 10ºC higher than for 4.5 wt% antimony. 2.75 wt% antimony and calcium-aluminium are in the same temperature range as calcium.
  4. Grid mould. Again, temperatures need to be higher. The mould gate operates around 150ºC on antimony and about 200ºC on calcium. Both low antimony and calcium-aluminium run slightly hotter than 4.5 wt% antimony.
  5. Lower mould. The temperature for 4.5 wt% antimony is 170ºC while calcium must be processed at 204ºC. Again, calcium-aluminium and low antimony run slightly hotter (at 193ºC) than 4.5 wt% antimony.
  6. Upper mould. Temperature controls are not required on any of the alloys other than calcium. The upper-mould temperature for calcium is 204ºC, i.e., the same as for the lower mould.

Calcium-grid caster

Beginning at the lead pot, the lead pump should be a low rpm design. Gas shielding around the shaft reduces drossing; however, this must be supplied with gas at all times. Not doing so can be extremely dangerous with calcium-aluminium alloys. The lead pump may require special self-cleaning bushings, depending on the calcium alloy. Feedlines must be of the dead-head type with good insulation and heat controls. Lead dispensing valves should be gas shielded to prevent any oxidation taking place in the valve. The pouring ladle should be electrically heated automatically to maintain the proper lead temperature. The ladle also requires gas shielding to prevent dross build up. The amount of gas burning off is then very small and is contained in the ladle vent hood. By grinding the front face of the ladle, a wiper can be included. Dripping from the ladle into the mould is definite problem with calcium alloys and causes reduced production. Wirtz have developed a ladle wiper to wipe the lead from the ladle lip after each pour and thereby eliminate down times.

Once the grid is cast, the machine’s handling system must ensure that grid distortion does not occur. Ejection of the grid from the mould must be very precise. More ejector pins are required and mould design becomes more important. Since the alloy solidifies at 324ºC, the grids can be very hot when ejected from the mould. It is desirable to cool the pallet entry plate and trim die to remove heat quickly from the grid. In spite of these high temperatures, hot cracks are never a problem. Grids are either solid or liquid when ejected from the mould.

Other grid handling features have been developed by Wirtz for use with calcium alloys. One is the die-entry gate support assembly. Since calcium alloy is very soft and flimsy after casting, it tends to sag when entering the trim die due to the heavy gate on each grid. This sag produces a mis-trim (a crapped plate). The gate support assembly has a bar which supports each grid gate until the trim die engages the grid. It then moves away to allow the trim scrap to pass by it.

Another Wirtz feature is the die-entry roller assembly. The flimsy calcium feet easily bend if allowed to free fall into position in the trim die. Again, this binding causes mis-trims and scrap grids. The die-entry rollers support the grid and gently transport it to the trim. Die allowing it to fall only a short distance, thereby eliminating the problem

Trimming and stacking of the trimmed grid can be accomplished by conventional means, but the grid is still very soft. The trim die must be more precise to trim clean. The grid stacker is more critical and must handle the grid more gently in order to prevent distortion. Die-exit rollers have been added to eliminate any distortion caused by the free falls of the grids to the stacker. Exit rollers now support the grid and gently transfer it to the stacker rails.

The ability to handle the soft grid actually controls the casting speed. With the proper handling features, casting rates are equal to, or greater than, those achieved with low antimony alloys. Typically, calcium casters are operated at around 18 shots per minute, with some exceeding 20.

Grid moulds, need to be designed differently when the alloy is calcium. Calcium-grid moulds require more heat controls, more cooling capability, increased venting, different insulation allowances and improved ejection. Grid needs to be designed with more emphasis on lead flow and turbulence caused by lead. Tapers, radii and mould finish are all important features which must be considered by the mould maker. At higher mould temperatures, it is necessary to add heat by some means (e.g., electric heaters) and also to control the temperature of the mould cooling fluid. Corking grid moulds for calcium alloys is different from that with antimony alloys. Calcium alloys require a tighter, more durable cork that can withstand the higher lead temperatures and ejection of the soft calcium grid. Antimony-grid moulds are cut with cork allowances of 0.15 mm in the wires and 0.04 mm in the frames and on the surface. By comparison, calcium grid moulds are cut with the same amount cork allowance in the wires but with a greater amount on the surface and in the frames. Grid mould s designed for calcium alloy can be run with low antimony alloys at a slightly slower speed. However, antimony moulds do not function well on calcium alloys.

Present Status

State-of-the-art Wirtz casting machines can cast thin, lightweight grids from calcium or calcium-aluminium or 1 wt% antimony-lead alloys at speeds of up to 65 m per minute. They produce grid material with thickness variations of less than ±0.02 mm and weight variations of less than ± 1 g.

A steel-belt pasting machine has proven its ability to paste both stiff and soft paste on grid material as thin as 0.07 mm at speeds of 65 m per minute. Tolerance control of the pasted plates is within ± 0.05 mm or thickness. These tolerance controls are achieved by precision machine design and without the use of expensive computer control.

A high-speed rotary cutter is capable of cutting pasted strip into individual plates at speed of up to 65 m per minute at close tolerances.

At the present time, two continuous casting lines are being moved from engineering facilities to production plants. One of these systems will make calcium-alloy negative plates. The other system will make positive and negative plates from 1 wt% antimony alloy.