(a) The first thing to do is to put all of the information given on a common basis.Right now the compositions are in mole% but the flow rate of the hexanecondensate is a volumetric flow rate.
The easiest thing is to convert the hexanecondensate flow rate to a molar flow rate. From Appendix B.1 at the back of thetext we can find the density and molecular weight of hexane. Then

Adding values for the unknowns into the process flow diagram and noting thatwhatever is not hexane must be nitrogen in the two gaseous streams we get



A gas stream contains 18.0 mole% hexane and the remainder nitrogen. The stream flows to a...
Question: Solids soaked with liquid hexane are dried by being contacted with nitrogen at an elevated temperature. The gas stream leaving the dryer is at 80°C, 1 atm absolute and 50% relative saturation. (a) One of several possibilities for recovering the hexane from the gas is to send the stream to a cooling condenser. The gas stream leaving the condenser would contain 5.00 moles% of hexane, and hexane condensate would be recovered at a rate of 1.50 kmol/min. The condenser...
Hexane is a non-polar solvent with a boiling point of 68 °C, and is therefore the solvent of choice for oil extraction. The recovery system removes most of the hexane vapors from the air entering various pieces of equipment in the hexane solvent extraction plant, before discharging that air to the atmosphere. A gas stream contains 18 mole % hexane and the remainder is air leaving the solvent recovery unit at 150 °C and 1 atm and flow into condenser,...
#1 Acetone is to be removed from a nitrogen stream in a process. In the first step of the process, the gas is compressed from 1 atm to 4 atm. In the second step, the gas is cooled at constant pressure to a temperature of 5°C in a condenser. Some of the acetone condenses to liquid in the condenser and the remaining gas leaves the condenser saturated with acetone. The gas fed to the process enters at 40°C and 85%...
Please solve and I will rate answer
A gas stream containing acetone in air flows from a solvent recovery unit at a rate of 142 L/s at 150°C and 1.3 atm. The stream flows into a condenser which condenses most of the acetone, and the liquid and gas outlet streams are in equilibrium at -18°C and 5.0atm. Shaft work is delivered to the system at a rate of 25.2kW to achieve the compression from 1.3 atm to 5.0 atm. To...
CONFIDENTIAL BKC/1617/BKF2343 QUESTION 1 An equimolar vapor mixture of n-pentane and n-hexane at 110°C and 1 atm is fed into a condenser at a rate of 200 L min When the feed is cooled and compressed in the condenser, some of the vapor is condensed. The products are separated and discharged in separate streams. The vapor and liquid products at the top and the bottom of the condenser are(in equilibrium at 60°C and pressure P mmHg. The vapor product stream...
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beed help calculating from wt% to moles in the reactor outlet
stream. the reactor outket shows a molar flow rate but the
percentages of the reactor outlet are in weight %. see the note in
parenthesis in the question. thanks
3. Methanol is produced by reacting carbon monoxide and hydrogen. A fresh feed stream containing CO and Hjoins a recycle stream and the combined stream is fed to a reactor. The reactor outlet stream flows at a rate of...
Methanol is produced by reacting CO and H2. A fresh feed stream containing CO and H2joins a recycle stream, and the combined stream is fed to a reactor. A portion of the methanol leaving the reactor is condensed, and the unconsumed CO and H2and uncondensed methanol are recycled. The stream going from the reactor to the condenser flows at a rate of 275 mol/min and contains 63.1 mole% H2, 27.4 mole% CO and 9.53 mole% CH3OH. The mole fraction of...
A gaseous stream containing 20.0 mole% ethanol and 80.0 mole% air is to be cooled from 60.0°C to 9.65°C in a condenser at the constant pressure of 1 atm to liquefy some of the ethanol. The gas stream entering the condenser has a pressure of 1.00 atm, flows at a rate of 10.0 mole/s and, at 60°C, is well above the saturation temperature (42.4°C). As a result of the cooling, 1.75 mole/s of liquid ethanol (Top = 78.5°C) leaves the...
A gaseous stream containing 20.0 mole% ethanol and 80.0 mole% air is to be cooled from 60.0°C to 9.65°C in a condenser at the constant pressure of 1 atm to liquefy some of the ethanol. The gas stream entering the condenser has a pressure of 1.00 atm, flows at a rate of 10.0 mole/s and, at 60°C, is well above the saturation temperature (42.4°C). As a result of the cooling, 1.75 mole/s of liquid ethanol (Top = 78.5°C) leaves the...
The stream "1" consisting of yP1 mole % propane and yEl mole % ethane is blended with the stream "2" containing propane alone and the stream "3"containing nitrogen alone in a mixer in order to produce a gas mixture at Qp inch'/hr. The gas mixture produced with the streams "I". "2", and "3" contains xPP mass % propane, XEP mas % ethane, and XNP mass % nitrogen. The pressure and temperature of the product stream are PtPpsig and TP®F, respectively....