Assume that two chemical species A and B, are in a solvent feedstream entering a liquid-phase continuous stirred tank reactor maintained at constant temperature. The two species react irreversibly to form a third species, P. Develop a mathematical model that describes how the concentration of each species changes with time. Assume that the stoichiometry of the reaction is as follows: A + 2B → P

question 3 in imageee

Thermodynamics of Warfarin binding to human plasma albumin.Warfarin (coumadin) binds to human plasma albumin to prevent blood clotting in the reactionMeasured thermodynamic values for this reaction at 25oC are ∆G =-30.8 kJ/mol, ∆H=-13.1 kJ/mol, and ∆Cp~0.(a) Determine the entropy change for this reaction at 25oC.(b) Determine the fraction of unbound albumin over a temperature range of 0 to 50oC for a solution initially containing warfarin and albumin at 0.1 mM.

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Please try to solve in Extent Reaction or Molecular balance way. My professor wants to have the answer in that way not normal chemistry x y way. Thank you.

1) Ethanol-Water Separations. We wish to separate ethanol from water in a sieve-plate distillation column with a total condenser and a partial reboiler. There are two feed streams: Thermal State subcooled liquid* saturated vapor *Feed 2 condenses 0.25 moles of vapor for every mole of feed. The bottoms product should be 2% (mol) ethanol and the distillate should be 72% (mol) ethanol. Feed Flowrate (mol/hr) ZF 1 0.4 2 0.3 200 300 Notes: • The reflux ratio is equal to (1.0) and the feeds are to be input at their optimum location(s). • Both feeds are being input into the column, e.g. this is not intended to be solving for two unique columns but just one that has two input feed streams. • Equilibrium data for Ethanol-Water at 1 bar is shown in the table. You may also identify /use other experimental data (web sources, library) for this system. a) What are the flowrates of the distillate and bottoms products? b) What are the flowrates of liquid and vapor on stages between the two feeds…

Analytical solution of reactor design equation: Consider the irreversible reaction, which occurs in the gas phase, under isothermal and isobaric conditions: A  +  B →  2C  + D The applicable rate law (non-elementary) is –rA= kCACB.  Assume A is the limiting reactant. Write out the full rate law expressionas a function of conversion XA, given FA0= 1 moles/min and FB0= 3 moles/min (inlet molar flow of products is zero). Show this rate expression two times, one with parameters only (no numbers substituted in) and the second with all known or calculated values inserted. What is the PFR reactor volumerequired to achieve a conversion of XA= 85% if the influent volumetric flow rate (v0) is 5 L/minute and the reaction rate constant k = 2.2 (L/moles) minutes-1?   Develop your solution by performing the analytical integration of the differential equation, using integration tables in Appendix A of the textbook.  Credit will not be given for part (b) of this problem unless the solution is shown…

Problem 3 Dibutyl phthalate (diester) is produced in a CSTR operated isothermally at 112°C. The rate of formation of the di-ester from phthalic anhydride and butanol being very fast, the controlling step, in the presence of sulphuric acid catalyst, is the conversion of mono-ester to the diester. The liquid phase reaction is: СЫН.(СООCН:)CООН + CН,ОН A C6H4(COOC4H6)2 + H2O D B The rate of the reaction is given by the expression -TA = kC; gmol/L.h where CA is the concentration of the mono-ester in gmol/L. The value of the apparent rate constant is given by: k = 0.7628 x 10ol1.965- L/gmol.h where T is the reaction temperature in K. The initial concentration of the mono-ester is 2.84 gmol/L and the density of the reaction mixture is 0.984 kg/L. (Molar mass of diester = 278) 1. In an existing plant consisting of a CSTR of 1.1 m diameter and 1.6 m height, the volumetric feed rate is 10 L/min. (a) Find the conversion achieved in an ideal CSTR. (b) If the conversion achieved in practice 68.5%…

i need help with both of the parts of this question

Consider the reaction below to be at equilibrium: 4 A(e) + 3 B(e) + heat 5 Ce) + 3 D(e) In which direction will the reaction shift if more D is added? O It will not shift O It will shift toward the products. O It will shift toward the reactants.