(a) Consider the reactions to be liquid phase and plot the species côncentrations and the conver of A as a function of the distance (i.e., volume) down a 50-dm³ PFR. Note any maxima (b) Consider the reactions to be liquid phase and determine the effluent concentrations and conversion

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.

feedback to help with ques: Q4. Again, we know that the molar flux to and from the interface must be equal (no accumulation), and that there is equilibrium at the interface. Knowing the bulk mole fractions and film mass transfer coefficients allows us to solve for the other unknowns, including the compositions of vapour and liquid at the interface, y* and x*. A graphical approach is required since we are given the equilibrium line as a plot. ans Q4 XA *=0.28; yA *=0.67; NA=0.006 mol m-2 s-1 ans 4) A packed distillation column is used to separate methanol from water. At an intermediate height within the packed column, the mole fraction of methanol in the bulk of the vapour is 0.6 and the mole fraction of methanol in the bulk of the liquid is 0.4. Using the xy diagram overleaf, determine the molar flux of methanol from liquid to vapour at this vertical position in the column, given the film mass transfer coefficients, KG=0.1 mol m² s-1 and kL=0.05 mol m-² s-¹.

Q.1) In an air-CO2 mixture at 298k & 303.9 KN/m², the concentration of CO2 at two planes (2mm) apart are 20% & 30%. The diffusivity of CO2 under the 273 k and 101.3 KN/m² is (1.85 x 104 m²/s), calculate the rate of transfer of CO2 across the two planes assuming; a. Diffusion of CO2 through stagnant air layer . b. Equimolar counter diffusion

Given the following cell Pb, PbCl2; HCl (1m); AgCl,AgThe value of the electromotive force at 25oC is 0.4900 volt. The rate of change of the electromotive force with temperature is 0.000186 volt/degree. Calculate ∆H, ∆S, and ∆G for the reaction.

The following questions are in regard to the mass transfer  a.) If you have a system with the same soulute concentration everywhere, will mass transfer occur? b.) When will a bulk concentration equal an inerfacial concentration? When won't it? c.) What are typical units for partition coefficients?

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Experiments are conducted on the uptake of a water pollutant in water over an adsorbing solid. Once equilibrium is reached the concentration C, of the pollutant in the water (in mg/L) and the ratio Q of mass of adsorbing solid/mass of adsorbed pollutant (in g/mg) are measured. Experimental data are presented in the table below. These data are correlated using the following equation: where a and 8 are constants and: Cp is in mg/L Q is in g/mg a. Determine the units of oa and B in this equation: b. Appropriately transform the above equation using newly defined variables so that you can linearly regress the data visually to obtain the values of a and B. Cp (mg/L) Q (g/mg) 0.0049 1.3 0.0035 12.5 0.0027 75.2 0.0018 930.2

Please help me only 7,8,9,10 please....

Give two reasons (short statements) why the rate of a catalyzed reaction mightdecrease as the pressure of one of its products increases.