billbill20002000
Chemical
- Nov 4, 2001
- 15
Hello group
I am currently designing spreadsheets applications for unit operations, I have ready a multiple evaporator, packed adsorption colum sheets, but now I am working on a packed bed dryer. I have set up cells to calculate mass transfer coefficient, difussion coeficients, and humidity content in the solid. No I am atempting to predict the change in temperature and humidity content across the column by using:
for heat transfer
(h*a/G*cs) Integral(dz) = integral (dT/(T-Tw))
(h*a/G*cs)*(z - zo) = ln[(T1-Tw)/(T2-Tw)]
where h,a, G, cs are heat transfer coeff, dimension factor, flow rate per area, specific heat.
for mass transfer
(ky*a*M/G) integral(dz) = integral(dH/(Hw-H))
(ky*a*M/G)*(z-zo) = ln [(Hw-H2)/(Hw-H1)]
Where ky is mass transfer coefficient, H is humidity in gas stream use for drying.
My question is that since I migth have drying from a constant rate of drying to a falling rate of drying, how could I include this effect in the previous equations? I heard that I could use finite difference to solve this problem, but I have neither experience nor knowledge of numerical methods. any sugestions? do any of you know of a really practical book for num methods? the ones I checked have too much math and few examples that it just makes my confusion even bigger. Can this problem be solved analitically?
thanks
Cheers
Will
I am currently designing spreadsheets applications for unit operations, I have ready a multiple evaporator, packed adsorption colum sheets, but now I am working on a packed bed dryer. I have set up cells to calculate mass transfer coefficient, difussion coeficients, and humidity content in the solid. No I am atempting to predict the change in temperature and humidity content across the column by using:
for heat transfer
(h*a/G*cs) Integral(dz) = integral (dT/(T-Tw))
(h*a/G*cs)*(z - zo) = ln[(T1-Tw)/(T2-Tw)]
where h,a, G, cs are heat transfer coeff, dimension factor, flow rate per area, specific heat.
for mass transfer
(ky*a*M/G) integral(dz) = integral(dH/(Hw-H))
(ky*a*M/G)*(z-zo) = ln [(Hw-H2)/(Hw-H1)]
Where ky is mass transfer coefficient, H is humidity in gas stream use for drying.
My question is that since I migth have drying from a constant rate of drying to a falling rate of drying, how could I include this effect in the previous equations? I heard that I could use finite difference to solve this problem, but I have neither experience nor knowledge of numerical methods. any sugestions? do any of you know of a really practical book for num methods? the ones I checked have too much math and few examples that it just makes my confusion even bigger. Can this problem be solved analitically?
thanks
Cheers
Will