Subystud
Chemical
- Jan 12, 2012
- 60
Hello -
I am looking to design / sub-out a skid for diluting 93% H2SO4 to 50%. I have some questions regarding the heat balance.
1. From the enthalpy-concentration diagram, I obtained a value of -64 BTU/lb to do the dilution at the listed conditions.
Is this all the heat that needs to be accounted for?? Or, is this simply the delta_Enthalpy for 50% acid from 230F to 120F? Do I also need to consider the heat capacity of the sulfuric acid and the energy associated with lowering the temperature of the hot, diluted mixture from 230F to 120F?
2. Integral Heats of Mixing. These are listed as ratios of solute:acid in molar form at 25C. The energy that outputs from this equation is the energy that must be removed to get the final mixture at 25C. Is this correct?
I am having some difficulty on when to use what...
Thanks,
Rob
I am looking to design / sub-out a skid for diluting 93% H2SO4 to 50%. I have some questions regarding the heat balance.
1. From the enthalpy-concentration diagram, I obtained a value of -64 BTU/lb to do the dilution at the listed conditions.
Is this all the heat that needs to be accounted for?? Or, is this simply the delta_Enthalpy for 50% acid from 230F to 120F? Do I also need to consider the heat capacity of the sulfuric acid and the energy associated with lowering the temperature of the hot, diluted mixture from 230F to 120F?
2. Integral Heats of Mixing. These are listed as ratios of solute:acid in molar form at 25C. The energy that outputs from this equation is the energy that must be removed to get the final mixture at 25C. Is this correct?
I am having some difficulty on when to use what...
Thanks,
Rob