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the batch fermentation of glucose to glutamic acid using brevibacterium divaricate is described in detail in us patent
natural gas is widely used as fuel in the process industries so the price of natural gas is often an important variable
in a process for the production of acrylic fibers by the emulsion polymerization of acrylonitrile the unreacted monomer
the adipic acid plant described in examples 95 and 99 is to be built in china with a location factor of 085 the cost
acetylene is formed as a by-product in the manufacture of ethylene it is removed by selective hydrogenation using noble
a tablet forming process is to be continuously fed with 10 kgh of usp grade sorbitol powder when in operation the
styrene can be made by catalytic dehydrogenation of ethyl benzene the reaction is usually carried out in the presence
a plant is producing 10000 metric tons per year 10 kty or 10 kmta of a product the overall yield is 70 wt 07 kg of
differential energy balancein the batch preparation of an aqueous solution the water is first heated to 80 degc in a
the composition of a gas derived by the gasification of coal is volume percentage carbon dioxide 4 carbon monoxide 16
allyl alcohol can be produced by the hydrolysis of allyl chloride together with the main product allyl alcohol diallyl
in the production of ammonia from hydrogen and nitrogen the conversion based on either raw material is limited to 15
the product from a crystallizer is to be separated from the liquor using a centrifuge the concentration of the crystals
a preliminary class 4 estimate of the isbl capital cost of building a 200000 ton per year ethanol plant by corn dry
a gas produced as a by-product from the carbonization of coal has the following composition mole carbon dioxide 4
the vapor from a chlorine vaporizer will contain some liquid droplets the vaporizer consists of a vertical cylindrical
styrene is made by dehydrogenation of ethyl benzene which is formed by alkylation of benzene with ethylene propose
methyl ethyl ketone mek is manufactured by the dehydrogenation of 2-butanol using a shell and tube type reactor flue
a toluene surge drum has capacity 500 gal and is normally operated 60 full at 100 ordmf under 300 psig of hydrogen in
a what alarms would you add to the vaporizer control scheme shown in figure indicate whether the alarm would signal
a class 2 estimate of the isbl capital cost of building a 200000 mmlbyr ethylene cracking plant has been stated as 850
when heavy oils are cracked in a catalytic or thermal cracking process lighter hydrocarbon compounds are formed most
optimize the design of a distillation column to separate 225 metric tons per hour of an equimolar mixture of benzene
a supply of nitrogen is required as an inert gas for blanketing and purging vessels after generation the nitrogen is
it is proposed to use an existing distillation column which is fitted with a dephlegmator reflux condenser that has 200