Please show the plot coding using MATLAB ONLY! No Polymath or other software only Matlab!

The dehydration butanol of alumina is carried out over a silica-alumina catalyst at 680 K. The rate law is with k = 0.054 mol/gcathatm and KBu = 0.32 atm1. Pure butanol enters a thin-tubed, packed-bed reactor at a molar flow rate of 50 kmol/hr and a pressure of 10 atm (1013kPa). (a) What PBR catalyst weight is necessary to achieve 80% conversion in the absence of pressure drop? Plot and analyze X, p, f (i.e., (v/v0)) and reaction rate, , as a function of catalyst weight. (b) What fluidized CSTR catalyst weight is necessary to achieve 80% conversion? (c) Repeat (a) when there is pressure drop, with the pressure-drop parameter = 0.0006 kg1. Do you observe a maximum in the rate of reaction, and if so, why? What catalyst weight is necessary to achieve 70% conversion? Compare this weight with that for no pressure drop to achieve the same conversion. (d) What generalizations can you make about this problem?

4B The dehydration butanol of alumina is carried out over a silica-alumina catalyst at 680K. CH3CH2CH2CH2OHcatCH3CH=CHCH3+H2O The rate law is rBu=(1+KBuPBu)2kPBu with k=0.054mol/gcathatm and KBu=0.32atm1. Pure butanol enters a thin-tubed, packed-bed reactor at a molar flow rate of 50kmol/hr and a pressure of 10atm(1013kPa). (a) What PBR catalyst weight is necessary to achieve 80% conversion in the absence of pressure drop? Plot and analyze X,p,f( i.e., (v/v0)) and reaction rate, rA, as a function of catalyst weight. (b) What "fluidized CSTR" catalyst weight is necessary to achieve 80% conversion? (c) Repeat (a) when there is pressure drop, with the pressure-drop parameter =0.0006kg1. Do you observe a maximum in the rate of reaction, and if so, why? What catalyst weight is necessary to achieve 70% conversion? Compare this weight with that for no pressure drop to achieve the same conversion. (d) What generalizations can you make about this