Recovering and reusing organic solvents is an important part of the operation of most chemical plants. The magnitude of these recovery efforts can be staggering: e.g., in recent years Eastman Chemical Company used 4.0 billion pounds of solvents annually and recovered 3.96 billion pounds (99%). Eastman's installation of a $26 million (in 1990 dollars) acetone-recovery system reduced acetone emissions by 50% in the division that had been responsible for most of these emissions.⁹ A gas stream containing 20.0 mole% acetone and the remainder nitrogen leaves a chemical plant at 90°C and 1 atm. In an acetone-recovery process, stream is cooled at constant pressure in a condenser, enabling some of the acetone vapor to be recovered as a liquid. The nitrogen and uncondensed acetone are discharged to the atmosphere.

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Chapter1: Chemical Foundations
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. Recovering and reusing organic solvents is an important part of the operation of most chemical plants.
The magnitude of these recovery efforts can be staggering: e.g., in recent years Eastman Chemical
Company used 4.0 billion pounds of solvents annually and recovered 3.96 billion pounds (99%).
Eastman's installation of a $26 million (in 1990 dollars) acetone-recovery system reduced acetone
emissions by 50% in the division that had been responsible for most of these emissions.⁹
A gas stream containing 20.0 mole% acetone and the remainder nitrogen leaves a chemical plant
at 90°C and 1 atm. In an acetone-recovery process, stream is cooled at constant pressure in a
condenser, enabling some of the acetone vapor to be recovered as a liquid. The nitrogen and
uncondensed acetone are discharged to the atmosphere.
Transcribed Image Text:. Recovering and reusing organic solvents is an important part of the operation of most chemical plants. The magnitude of these recovery efforts can be staggering: e.g., in recent years Eastman Chemical Company used 4.0 billion pounds of solvents annually and recovered 3.96 billion pounds (99%). Eastman's installation of a $26 million (in 1990 dollars) acetone-recovery system reduced acetone emissions by 50% in the division that had been responsible for most of these emissions.⁹ A gas stream containing 20.0 mole% acetone and the remainder nitrogen leaves a chemical plant at 90°C and 1 atm. In an acetone-recovery process, stream is cooled at constant pressure in a condenser, enabling some of the acetone vapor to be recovered as a liquid. The nitrogen and uncondensed acetone are discharged to the atmosphere.
Two cooling fluids are available-cooling-tower water at 20°C and a refrigerant at -35°C. For
each fluid, calculate the percentage acetone recovery [(mol acetone condensed/mol acetone fed to
condenser) x100%], assuming that the condenser temperature equals the coolant temperature.
Transcribed Image Text:Two cooling fluids are available-cooling-tower water at 20°C and a refrigerant at -35°C. For each fluid, calculate the percentage acetone recovery [(mol acetone condensed/mol acetone fed to condenser) x100%], assuming that the condenser temperature equals the coolant temperature.
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