Process Calculations - Video Lectures on Short Theory, Problems with Detailed Solutions
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Material Balance with Reactions
Material Balance - Theory - part1 - video
Material Balance - Theory - part1 - slides
Material Balance - Theory - part2
Fuel Gas Mixture - Composition and Air Requirement
Combustion of Propane: Atomic Balance - Extent of Reaction - Workout
Formaldehyde from Methane - Extent of Reaction, Atomic Balance - Example
Formaldehyde from Oxidation of Methane - Another Explanation
Combustion of Pentane
Chlorination of Benzene
Combustion of Methane - Atomic Balance - Extent of Reaction
Analysis of Fuel Gas
Excess Air in Combustion of Propane
Chlorination of Carbondisulfide
Yield, Selectivity of Reactions
Yield and Selectivity - Dehydrogenation of Ethane
Yield and Selectivity - Ethylene Hydration Reaction
Yield, Conversion, Selectivity in CO Production from CH4
Theoretical and Excess Air - Example
Combustion of Coal
Combustion of Methanol
Ethylene Bromide from Ethylene
Air Requirement of Claus Plant
H/C of Fuel from Orsat Analysis
Conversion of SO2 in Secondary Converter
Flowrate of a Component from Conversion Data
Pressure vs. Conversion in a Batch Reactor
Fuel Composition from Dewpoint of Flue Gas
Methanol Production with Recycle
Methanol Production with Recycle and Purge
Methanol Production with Recycle and Purge - DoF Analysis, Atomic Balance and Extent of Reaction Methods
Acetaldehyde from Ethanol with Recycle
Ethanol from Ethylene - Recycle, Purge
Amount of Reactant in Purge
Material Balance with Reactions - Short Questions
Limiting Reactant and Percent Excess
Limiting Reactant and Percent Excess - Another Explanation
Volume of Gas Collected from Reaction of CaCO3 with HCl
Chlorine from NaCl Brine
Degree of Freedom Analysis for Combustion System
Conversion of a Reactant - Multiple Reactions
Conversion of Gaseous Reaction - Extent of Reaction and Volume Expansivity Factor Approaches
Excess Oxygen from Flue Gas Data
Excess Oxygen from Flue-gas Data - Another Explanation
Percent Excess Air from Flue-gas Composition
Composition of Wet Gas from Dry Gas Data
Composition of Feed for the Given Excess Air
Maximum Possible CO2 in Flue-gas from CH4 Combustion
Composition of Reactor Exit for the given Conversion
Degree of Completion of Reaction
Single-pass and Overall Conversions - Ex-1
Single-pass and Overall Conversions - Ex-2
Recycle Rate for the given Conversion
Feed to Recycle Ratio for the given Conversion
Composition of Product from the given Conversion
K
2
O Equivalent of KCl
CaO from Limestone
Concentration of Solutions
Coal Sample Analysis
Material Balance without Reaction
Blending of Two Liquid Streams
Weight Loss due to Breathing
Preparation of Mixed Acid
Mixed Fertilizer Formulation
Preparation of Sulfuric Acid Solution
Removal of Water by Bubbling Air
Removal of Hexane from Gas by Condensation
Loss of Octane due to Vaporization
Drying of CaCO3 Slurry
Condensation of Moisture from Compressed Air
Condensation of Moisture in Air-Conditioning Process
Adsorber for Moisture Removal
Bypass for RO
Evaporation of Spent Lye
Capacity of Evaporator
Solute Dissolution in Solvent
Preparation of Saturated MnSO4 Solution
Crystallization of Na2SO4
Unsteady Mass Balance - Salt Dissolution
Material Balance without Reaction - Short Questions
Molecular Formula from Composition Data
Mass Fraction to Mole Fraction
Degree of Freedom Analysis for a Splitter
Volume of Gas Required for a Given Composition
Recovery of Oil by Extraction - Ex-1
Recovery of Oil in Extraction - Ex-2
Drying of Solid
Evaporation - Mass Balance
Solubility of Salt
Moles of a Compound for a Mass Fraction
Molarity of Sulphuric Acid Solution
Energy Balance Calculations
Theory with Examples
Steam Mixing
Adiabatic Mixing of Steam
Temperature vs Time Curve for Heating of Water
Heat of Formation from Heat of Combustion Data
Heat of Reaction from Heat of Combustion
Heat of Reaction at Constant Volume
Amount of Heat Transferred to Reactor
Heat Released from Reaction
Adiabatic Flame Temperature of Natural Gas Combustion
Maximum Allowable Conversion of Exothermic Reaction
Heat Loss from the Combustion System
Isothermal Operation of Combustor to Convert Carbon and CO2 to CO
Calorific Value of Fuels
Heat Transferred from Reactor
Adiabatic Combustion of Methane
Heat Released from Combustion of CO
Rate of Heat Removal from Ammonia Oxidizer
Heat Removed from Ammonia Oxidizer - Multiple Reactions
Temperature of Ammonia Oxidizer
Energy Balance for Production of Acetylene from Methane
Energy Balance for Production of Acetylene - Another Explanation
Exit Temperature of Flue Gas
Excess Air and Adiabatic Flame Temperature
Quick Review of Theory
Quick Review of Material Balance
Material Balance - Theory
Material Balance - Examples
Quick Review of Energy Balance
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