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➢ Proposed process was significantly cost effective (60% lower capital cost), energy efficient (200% lower cooling cost), more productive (30% better hydrogen uptake) and safer (operated at 3-4 times lesser pressure).
➢ Proposed new green process was significantly cost effective (25% lower capital cost), energy efficient (50% lower energy requirement), more productive (50% less purge) and had higher catalyst life and by-product output.
➢ Process achieved significant reduction of the water separation footprint (20%), produced pipeline transportable oil without diluent and purified the emulsified water without massive water treatment.