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all about aeration in water system
limitation of its
ac++ programming which calculate molcular weight of hydrocarbon compounds
complete phase rule assignment
Factors affecting on process design
How do u think the appropriate enzyme would have affected the reaction
A shell-and-tube Heat exchanger with one shell exceed and two tube passes si to be designed to condense 3900 kg/hr of steam at 1 atm. Steam may be suppose to enter the shell side a
heat exchanger would be difficult to model
develop a process schematic which will yield separation process streams
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