Thank you. Please upvote it. ??
i beed help calculating from wt% to moles in the reactor outlet stream. the reactor outket...
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...
Problem 4.80 Methanol Synthesis Methanol is synthesized from carbon monoxide and hydrogen in a catalytic reactor. The fresh feed to the process contains 32.0 mol% CO 64.0 mol% H2 and 4.00 mol% N2: This stream is mixed with a recycle stream in a ratio of 10.00 mol recycle / mol fresh feed to produce th feed to the reactor, which contains 12.0 mol% N2 The reactor effluent goes to a condenser from which two streams emerge: a liquid product stream...
Methanol is synthesized from carbon monoxide and hydrogen (H2) in a catalytic reactor. CO + 2H2 → CH3OH The fresh feed to the process contains 32.0% mol of CO, 64% of H2 and 4% N2. This stream is mixed with a recirculation stream at a ratio of 5 mol recirculation / 1 mol fresh feed to the process. The mixture of these streams forms the feed stream to the reactor, which contains 13.0 mol% of N2. Low conversion is achieved...
Carbon monoxide and hydrogen react catalytically to produce methanol. CO + 2HZ rightarrow CH_3OH The fresh feed (100 moles/min) composition is 30 mole% carbon monoxide, a stoichiometric proportion of hydrogen and 10 mole% inert (nitrogen). A condenser (operates at 0 degree C and 1 atm) separates the unreacted gases and inert from the liquid product methanol. Part of the gas stream is recycled back into the main feed line to the reactor and the rest purged. The recycle ratio is...
me liquid methanol condensate is withdrawn as a product, and the gas stream leaving the ondenser, which contains CO, H2, and 0.40 mol% CH3OH, is the recycle stream that combines ith the fresh feed. a. Draw and label the flow diagram. (2 marks) b. Calculate the fresh feed rates of CO and H2 (5 marks) Hint: don't start with the overall process balances as the equations are not independent. c. Calculate the single pass and the overall all conversion of...
Terephthalic acid (TPA) is synthesized from -xylene (PX) in the process C8H10 +302 – C8H6O4 +2H2O shown below. A fresh feed of pure liquid PX combines with a recycle stream containing PX and a solution (S) of a catalyst (a cobalt salt) in a solvent (methanol). The combined stream, which contains S and PX in a 3:1 mass ratio, is fed to a reactor in which 90% of the PX is converted to TPA. A stream of air at 25...
A gas stream contains 18.0 mole% hexane and the remainder nitrogen. The stream flows to a condenser, where its temperature is reduced and some of the hexane is liquefied. The hexane mole fraction in the gas stream leaving the condenser is 0.0500. Liquid hexane condensate is recovered at a rate of 1.50 L/min. (a) What is the flow rate of the gas stream leaving the condenser in mol/min? (Hint : First calculate the molar flow rate of the condensate and...
4. In the production of soybean oil, beans containing 18.0 wt% oil and 82.0 wt% solids are ground and fed to a stirred tank (also called an extractor), along with a stream of liquid n containing recycled hexane and fresh hexane. The feed ratio is 4.2 kg hexane/kg beans. ground beans are suspended in the liquid, and essentially all of the oil in the beans is ex into the hexane. The stream exiting the extractor (also called the effluent) passes...
A synthesis gas stream consisting of 65.30% H2, 34.30% CO, and 0.400% CH4 (by mole) is fed into the process described below at a rate of 100 mol/hour. The effluent stream from the reactor is fed into a separator where the methanol is completely removed, and the unconverted reactants are recycled to the reactor. To avoid the buildup of methane, a portion of the recycled stream is purged. At present operating conditions, the CO conversion over the entire process is...
12 3. (35 pts) Ammonia (NHa) is synthesized from nitrogen and hydrogen. Fresh feed, which contains only N2 and H2, is blended with a recycle stream containing the same species composition of the mixture entering the reactor contains 50% excess H2 The fractional conversion of N2 in the reactor operated at T = 400°C, P = 2000 psig isXu2-05. Allspecie exit ammonia as a pure liquid and recycles the volatile components the reactor in the gas phase and are directed...