Reactant Conversion at Non Adiabatic Conditions Solution

STEP 0: Pre-Calculation Summary
Formula Used
Reactant Conversion = ((Mean Specific Heat of Unreacted Stream*Change in Temperature)-Total Heat)/(-Heat of Reaction per Mole at Temperature T2)
XA = ((C'*∆T)-Q)/(-ΔHr2)
This formula uses 5 Variables
Variables Used
Reactant Conversion - Reactant Conversion gives us the percentage of reactants converted into products, displayed as the percentage as a decimal between 0 and 1.
Mean Specific Heat of Unreacted Stream - (Measured in Joule per Kilogram per K) - Mean Specific Heat of Unreacted Stream is the heat required to raise the temperature of one gram of a substance by one Celsius degree of the unreacted reactant after reaction occurred.
Change in Temperature - (Measured in Kelvin) - The Change in Temperature is the difference between the initial and final temperature.
Total Heat - (Measured in Joule Per Mole) - Total Heat is the heat in the system.
Heat of Reaction per Mole at Temperature T2 - (Measured in Joule Per Mole) - Heat of Reaction per Mole at Temperature T2 is change in enthalpy at T2.
STEP 1: Convert Input(s) to Base Unit
Mean Specific Heat of Unreacted Stream: 7.98 Joule per Kilogram per K --> 7.98 Joule per Kilogram per K No Conversion Required
Change in Temperature: 50 Kelvin --> 50 Kelvin No Conversion Required
Total Heat: 1905 Joule Per Mole --> 1905 Joule Per Mole No Conversion Required
Heat of Reaction per Mole at Temperature T2: 2096 Joule Per Mole --> 2096 Joule Per Mole No Conversion Required
STEP 2: Evaluate Formula
Substituting Input Values in Formula
XA = ((C'*∆T)-Q)/(-ΔHr2) --> ((7.98*50)-1905)/(-2096)
Evaluating ... ...
XA = 0.718511450381679
STEP 3: Convert Result to Output's Unit
0.718511450381679 --> No Conversion Required
FINAL ANSWER
0.718511450381679 0.718511 <-- Reactant Conversion
(Calculation completed in 00.004 seconds)

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Anurag Group of Institutions (AGI), Hyderabad
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9 Temperature and Pressure Effects Calculators

Final Temperature for Equilibrium Conversion
Go Final Temperature for Equilibrium Conversion = (-(Heat of Reaction per Mole)*Initial Temperature for Equilibrium Conversion)/((Initial Temperature for Equilibrium Conversion*ln(Thermodynamic Constant at Final Temperature/Thermodynamic Constant at Initial Temperature)*[R])+(-(Heat of Reaction per Mole)))
Initial Temperature for Equilibrium Conversion
Go Initial Temperature for Equilibrium Conversion = (-(Heat of Reaction per Mole)*Final Temperature for Equilibrium Conversion)/(-(Heat of Reaction per Mole)-(ln(Thermodynamic Constant at Final Temperature/Thermodynamic Constant at Initial Temperature)*[R]*Final Temperature for Equilibrium Conversion))
Adiabatic Heat of Equilibrium Conversion
Go Heat of Reaction at Initial Temperature = (-((Mean Specific Heat of Unreacted Stream*Change in Temperature)+((Mean Specific Heat of Product Stream-Mean Specific Heat of Unreacted Stream)*Change in Temperature)*Reactant Conversion)/Reactant Conversion)
Heat of Reaction at Equilibrium Conversion
Go Heat of Reaction per Mole = (-(ln(Thermodynamic Constant at Final Temperature/Thermodynamic Constant at Initial Temperature)*[R])/(1/Final Temperature for Equilibrium Conversion-1/Initial Temperature for Equilibrium Conversion))
Equilibrium Conversion of Reaction at Initial Temperature
Go Thermodynamic Constant at Initial Temperature = Thermodynamic Constant at Final Temperature/exp(-(Heat of Reaction per Mole/[R])*(1/Final Temperature for Equilibrium Conversion-1/Initial Temperature for Equilibrium Conversion))
Equilibrium Conversion of Reaction at Final Temperature
Go Thermodynamic Constant at Final Temperature = Thermodynamic Constant at Initial Temperature*exp(-(Heat of Reaction per Mole/[R])*(1/Final Temperature for Equilibrium Conversion-1/Initial Temperature for Equilibrium Conversion))
Reactant Conversion at Adiabatic Conditions
Go Reactant Conversion = (Mean Specific Heat of Unreacted Stream*Change in Temperature)/(-Heat of Reaction at Initial Temperature-(Mean Specific Heat of Product Stream-Mean Specific Heat of Unreacted Stream)*Change in Temperature)
Reactant Conversion at Non Adiabatic Conditions
Go Reactant Conversion = ((Mean Specific Heat of Unreacted Stream*Change in Temperature)-Total Heat)/(-Heat of Reaction per Mole at Temperature T2)
Non Adiabatic Heat of Equilibrium Conversion
Go Total Heat = (Reactant Conversion*Heat of Reaction per Mole at Temperature T2)+(Mean Specific Heat of Unreacted Stream*Change in Temperature)

Reactant Conversion at Non Adiabatic Conditions Formula

Reactant Conversion = ((Mean Specific Heat of Unreacted Stream*Change in Temperature)-Total Heat)/(-Heat of Reaction per Mole at Temperature T2)
XA = ((C'*∆T)-Q)/(-ΔHr2)

What are Non Adiabatic Conditions?

Non-Adiabatic conditions are conditions which does not occur without loss or gain of heat, there will be some heat gaining or losing.

How to Calculate Reactant Conversion at Non Adiabatic Conditions?

Reactant Conversion at Non Adiabatic Conditions calculator uses Reactant Conversion = ((Mean Specific Heat of Unreacted Stream*Change in Temperature)-Total Heat)/(-Heat of Reaction per Mole at Temperature T2) to calculate the Reactant Conversion, Reactant Conversion at Non Adiabatic Conditions formula is defined as conversion of the reactant achieved at the conditions that does not occur without loss or gain of heat, there will be some heat gaining or losing. Reactant Conversion is denoted by XA symbol.

How to calculate Reactant Conversion at Non Adiabatic Conditions using this online calculator? To use this online calculator for Reactant Conversion at Non Adiabatic Conditions, enter Mean Specific Heat of Unreacted Stream (C'), Change in Temperature (∆T), Total Heat (Q) & Heat of Reaction per Mole at Temperature T2 (ΔHr2) and hit the calculate button. Here is how the Reactant Conversion at Non Adiabatic Conditions calculation can be explained with given input values -> 0.333492 = ((7.98*50)-1905)/(-2096).

FAQ

What is Reactant Conversion at Non Adiabatic Conditions?
Reactant Conversion at Non Adiabatic Conditions formula is defined as conversion of the reactant achieved at the conditions that does not occur without loss or gain of heat, there will be some heat gaining or losing and is represented as XA = ((C'*∆T)-Q)/(-ΔHr2) or Reactant Conversion = ((Mean Specific Heat of Unreacted Stream*Change in Temperature)-Total Heat)/(-Heat of Reaction per Mole at Temperature T2). Mean Specific Heat of Unreacted Stream is the heat required to raise the temperature of one gram of a substance by one Celsius degree of the unreacted reactant after reaction occurred, The Change in Temperature is the difference between the initial and final temperature, Total Heat is the heat in the system & Heat of Reaction per Mole at Temperature T2 is change in enthalpy at T2.
How to calculate Reactant Conversion at Non Adiabatic Conditions?
Reactant Conversion at Non Adiabatic Conditions formula is defined as conversion of the reactant achieved at the conditions that does not occur without loss or gain of heat, there will be some heat gaining or losing is calculated using Reactant Conversion = ((Mean Specific Heat of Unreacted Stream*Change in Temperature)-Total Heat)/(-Heat of Reaction per Mole at Temperature T2). To calculate Reactant Conversion at Non Adiabatic Conditions, you need Mean Specific Heat of Unreacted Stream (C'), Change in Temperature (∆T), Total Heat (Q) & Heat of Reaction per Mole at Temperature T2 (ΔHr2). With our tool, you need to enter the respective value for Mean Specific Heat of Unreacted Stream, Change in Temperature, Total Heat & Heat of Reaction per Mole at Temperature T2 and hit the calculate button. You can also select the units (if any) for Input(s) and the Output as well.
How many ways are there to calculate Reactant Conversion?
In this formula, Reactant Conversion uses Mean Specific Heat of Unreacted Stream, Change in Temperature, Total Heat & Heat of Reaction per Mole at Temperature T2. We can use 1 other way(s) to calculate the same, which is/are as follows -
  • Reactant Conversion = (Mean Specific Heat of Unreacted Stream*Change in Temperature)/(-Heat of Reaction at Initial Temperature-(Mean Specific Heat of Product Stream-Mean Specific Heat of Unreacted Stream)*Change in Temperature)
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