Question

mass perc to mola flow In the production of a drug having a molecular weight of...

mass perc to mola flow

In the production of a drug having a molecular weight of 28.7, the aqueous exit stream from the reactor flows at the rate of 10.9 L/min. The drug concentration is 42%, and the specific gravity of the solution is 1.079. Calculate the flow rate of the drug in kmol/min.

Homework Answers

Answer #1

PM=28,7

Q=10,9L/min

ge=1,079

ge= ρmixture/ρreference

Since it is a liquid mixture, the reference water density 1kg / L is taken

ρmixture=ge.ρmixture=1kg/L.1,079= 1,079kg/L

ρ=mass/Volume

Taking into account a calculation based on 1 minute

massmixturemixture.Volumemixture=1,079kg/L.10,9L= 11,7611kg

Concentration=massdrugx100/massmixture

massdrug=concentrationxmassmixture/100= (42x11,7611kg)/100= 4,9397kg

molesdrug=massdrug/PMdrug= 4,9397kg/(28,7kg/kmol)=0,1721kmol

it returning calculation based is obtained the flow rate of the drug in kmol/min = 0,1721kmol/min

Know the answer?
Your Answer:

Post as a guest

Your Name:

What's your source?

Earn Coins

Coins can be redeemed for fabulous gifts.

Not the answer you're looking for?
Ask your own homework help question
Similar Questions
The conversion of ferrous ions to ferric ions by dissolved oxygen in the presence of bacteria...
The conversion of ferrous ions to ferric ions by dissolved oxygen in the presence of bacteria is a first order reaction with respect to ferrous ions in the concentration range of 0.1 – 0.6 mol L-1 . The rate of oxidation of 0.6 mol L-1 ferrous ions is 0.25 mol L-1 min-1 . Calculate the following: (a) First order rate constant for the oxidation reaction. (b) Time taken for 70% conversion of ferrous ions at an initial concentration of 0.6...
In the absorption of component A (molecular weight = 60 g/mol) from an airstream into an...
In the absorption of component A (molecular weight = 60 g/mol) from an airstream into an aqueous solution, the bulk compositions of the two adjacent streams at a point in the apparatus were analyzed to be PA,G = 0.1 atm and CA,L = 1 kmol of A/m3 . The Henry’s Law constant was 0.85 ATM/mole fraction. The overall gas coefficient was KG = 0.27 kmol/m2/h/ATM. If 60% of the total resistance to mass transfer resides in the gas film, determine:...
A process off-gas flow contains 1,4 mol-% acetone, when the gas flow rate is 2,20 kmol/min....
A process off-gas flow contains 1,4 mol-% acetone, when the gas flow rate is 2,20 kmol/min. The acetone should be removed to achieve a concentration of 0,070 mol-% acetone in the outlet gas flow. The gas is washed with pure water with a flow rate 1,05 kmol/min. Calculate the acetone concentration (mol-%) of the spent washing liquid and the flow rate (mol/min) of acetone flowing from the gas phase to the aqueous phase
A perfectly mixed flow reactor is to be used to carry out the exothermic isomerisation reaction...
A perfectly mixed flow reactor is to be used to carry out the exothermic isomerisation reaction A -> R. The rate is given by: (-rA) = kCA (1st order) where k = 4 × 106e-8000/T s-1, where T is in K. The enthalpy of reaction ?HR = -167,480 kJ kmol-1 The molecular mass MA (=MR) = 100 kg kmol-1 CA0 initial concentration of A = 1 kmol m-3 For a temperature of 100°C and a production rate of R of...
1. An aqueous solution of sulfuric acid (6M H2SO4 in water) is flowing into a tank...
1. An aqueous solution of sulfuric acid (6M H2SO4 in water) is flowing into a tank at the rate of 100 liters/min (also can be written 100 L/min) having a density of 1.34 g/cm3. Calculate value of the items requested below and make sure you show HOW you obtained them. For parts (b) - (d), first write out the equation using symbols for the appropriate variables, and then algebraically solve for the unknown variables, and finally substitute in the numerical...
In a mass balance analysis, the mass flow rate (or rate of change of mass) due...
In a mass balance analysis, the mass flow rate (or rate of change of mass) due to a zero order generation reaction at a given point in time is 5625 mg/day. The reactor volume is 75.0 L. At the same point in time, the reactant concentration is 25.0 mg/L and the product (which is the material being analyzed in this mass balance) concentration is 10.0 mg/L. What is the zero order rate constant? Report your result in the units that...
Consider a 20 * 105 m3 lake fed by a polluted stream having a flow rate...
Consider a 20 * 105 m3 lake fed by a polluted stream having a flow rate of 4.2 m3/s and pollutant concentration equal to 25 mg/L. There is also a sewage outfall that discharges 0.5 m3/s of wastewater having a pollutant concentration of 275 mg/L. The stream and sewage wastes have a second order decay rate of 0.32/day. Assuming the pollutant is completely mixed in the lake and assuming no evaporation or other water losses or gains, find the steady-state...
8- The mass flow rate of the first gaseous feed stream, containing the component I only...
8- The mass flow rate of the first gaseous feed stream, containing the component I only , is 6,000 g\s .The total volumetric flow rate of the second gaseous feed stream, containing 67w%A and 33 wt%B,is 8,000 liter/s at 15 atm and 300k. These two gaseous feed streams are mixed and combined ,and then the combined gaseous feed stream is fed into a flow reactor at 420 k and 10 atm. All the componets are assumed to be ideal gases....
A natural gas mixture of methane (CH4) and ethane (C2H6) are used for the fuel source...
A natural gas mixture of methane (CH4) and ethane (C2H6) are used for the fuel source for generation of steam in a refinery plant.In this process,The gas stream mixture 1000kg/min having 70wt% CH4 and 30wt% C2H6 is burned with 100% excess air.Gas analysis shows that the CH4 and 85% C2H6 are completely burned into carbon dioxide , while 10% C2H6 is partially burned into carbon monoxide and the remaining C2H6 is unreacted. Assume the air stream feed to the furnace...
1. A combustion chamber is fed with 50 kmol/h of butane and 2000 kmol/h of air....
1. A combustion chamber is fed with 50 kmol/h of butane and 2000 kmol/h of air. Calculate the % excess air used and composition of the gases leaving combustion reactor, assuming complete combustion of butane. 2. In manufacture of chlorine, feed containing hydrochloric acid gas and air are fed to the reactor. The product gases leaving the reactor are found to contain 13.2% HCl, 6.3% 02, 42.9% N2, 30% Cl2 and 7.6% H2O (by weight). Calculate: i) The percent excess...