Abstract: The present invention relates to a product Kappaphycus alvarezii seaweed sap free of Gibberellic acid (GA3) and its method of preparation. Kappaphycus alvarezii seaweed sap is a plant stimulant found to enhance yield and quality of a number of crops. Besides containing many macro- and micro-nutrients, there are many plant growth hormones present in Kappaphycus alvarezii sap. It has been observed that pristine Kappaphycus alvarezii sap and GA3 free sap enhanced grain yield but surprisingly selective removal of GA3 from the pristine sap had profound stimulating effect on total dry above ground biomass yield of maize over and above the pristine sap. Upon seed treatment with GA3 free sap, ?-amylase enzyme activity in the germinating seed of mung bean is found to be increased. The foliar spray of GA3 free sap on tomato plants upregulated disease responsive genes (PR-3 and PR-5) as compared to pristine sap.

Abstract: The invention teaches the obtained specifications and process of production of engine worthy marine microalgal fatty acid methyl ester (biodiesel) using naturally occurring marine microalgal mats and also marine microalgae cultivated in cost-effective manner in solar salt pans. Utility of co-product streams adds to the attractiveness of the invention.

Abstract: A process for the production of high density hydration resistant sintered lime which comprises washing limestone having impurities of less than 2% to remove external impurities, crushing the washed limestone to a size of 25 mm or below, calcining the limestone at a temperature in the range of 1000 to 1150° C. for a period in the range of 2 to 3 hours to form a calcined mass, hydrating the calcined mass, drying the hydrated mass by known methods, deagglomerating the dried hydrated mass with 1 to 4 weight percent of an additive selected from the group consisting of a transition metal oxide capable of forming a low melting compound, a rare earth metal oxide capable of forming a solid solution, and mixtures thereof, pelletizing the resultant mixture at a pressure of at least 1000 Kg/lcm2, sintering the pellets at a temperature In the range of 1500° C. to 1650° C. for a period In the range of 24 hours and allowing the resultant sintered pellets to cool.