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Introduction to Chemical Engineering-II

Introduction to Chemical Engineering-II banner
Self-paced Beginner

Introduction to Chemical Engineering-II

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1691 min
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English
702 views
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What enrolled engineers say

3 verified reviews
  • May 3, 2026

    Doesn’t dodge the messy bits, but the labs assume you’ve already got MATLAB and Aspen wired up; that tripped me for an hour. After that, the material clicked. The McCabe–Thiele walkthrough in the distillation chapter stuck, especially the moment where they force a bad reflux choice and show the stage count blow up. That’s the kind of failure-mode thinking I expect in prod, not just tidy equations. The heat exchanger section tying LMTD back to fouling felt like infra obs, not theory. I’m not shipping PRs for k8s here, but the arch thinking translates. It nudged my baseline from “adequate” toward actually competent without pretending chemicalpharmaceutical work is clean.

    Saitheja A. Verified
  • May 3, 2026

    the McCabe-Thiele distillation lecture stuck; the VLE plot clicked, but I wasn't sold on the rushed reactor design homework.

    ajithkumar K. Verified
  • May 3, 2026

    The bias toward doing things the right way instead of shortcut math shows up early, which I tend to value when material bleeds into real systems. It frames Chem Eng II less as plug-and-chug and more like an arch problem, mapping assumptions, constraints, and failure modes—similar to how prod infra behaves when RPS spikes. The moment that stuck was Chapter 4’s McCabe–Thiele walkthrough on benzene–toluene, especially the step where the operating line shifts after changing reflux; that’s the kind of concrete knob-turning I remember. Mostly works, though I wasn't sold on the pacing around mass transfer coefficients; it jumps a bit and could use one more sanity-check example. There’s a steady emphasis on checking units and bounds, which felt like CI for equations, not flashy but keeps bad PRs out of the repo. It got across ideas I usually end up pulling from a senior in the hallway, minus the calendar ping.

    SYED HAMZA I. Verified

Is this course for you?

You should take this if

  • You work in Chemical
  • You're a Chemical & Process professional
  • You prefer self-paced learning you can revisit

You should skip if

  • You need a different specialisation outside Chemical & Process
  • You need live interaction with an instructor

Course details

This course provides a comprehensive introduction to the principles and practices of chemical engineering. Students will learn about the fundamental concepts of chemical engineering, including material and energy balances, thermodynamics, and transport phenomena. The course will also cover the application of chemical engineering principles to real-world problems, including process design, optimization, and safety.

Source - Youtube Channel (Andrew Paluch)

Course suitable for

Key topics covered

- Pure Fluids

- Equations of states

- Clapeyron Equations

- Phase behaviour of mixture

- Partial Molar properties

- Properties of mixing of ideal gases

-Theory of vapor liquid equilibirum

- Fugacity in mixtures

- Excess Enthalpy

- Activity Coefficients

- Ideal solutions

Course content

The course is readily available, allowing learners to start and complete it at their own pace.

96 lectures28 hr 11 min
  1. VLE of Pure Fluids - 1
    19 min
  2. VLE of Pure Fluids - 2
    8 min
  3. VLE of Pure Fluids - 3
    21 min
  4. Clapeyron Equation Derivation
    21 min
  5. Clausius/Clapeyron Example 1
    15 min
  6. Clausius/Clapeyron Example 2
    17 min
  7. VLE of Pure Fluids - 4
    17 min
  8. VLE of Pure Fluids - 5
    18 min
  9. Fugacity and Phase Equilibria
    7 min
  10. VLE of Pure Fluids - 6
    16 min
  11. Equation of State and VLE Example 1
    5 min
  12. Equation of State and Fugacity Example 1
    7 min
  13. Pure Component VLE using SRK Example 1
    8 min
  14. VLE of Pure Fluids - 7
    24 min
  15. Poynting Correction
    11 min
  16. Computing Fugacity Using Lee/Kesler Example 1.
    17 min
  17. Predicting VLE Using Cubic Equations of State
    23 min
  18. Predicting VLE Using Cubic Equations of State
    8 min
  19. Phase Behavior of Mixtures - 1
    8 min
  20. Phase Behavior of Mixtures - 2
    13 min
  21. Phase Behavior of Mixtures - 3
    12 min
  22. Phase Behavior of Mixtures - 4
    12 min
  23. Binary Txy Flash Example 1
    16 min
  24. Example problem using tabulated Txy data
    25 min
  25. Binary Txy Flash Example 2
    22 min
  26. Example problem using tabulated Pxy data
    20 min
  27. Phase Behavior of Mixtures - 5
    20 min
  28. Phase Behavior of Mixtures - 6
    15 min
  29. Phase Behavior of Mixtures - 7
    11 min
  30. Phase Behavior of Mixtures - 8
    19 min
  31. Phase Behavior of Mixtures - 8b
    19 min
  32. Binary VLLE Example 1
    27 min
  33. Binary VLLE Example 2
    19 min
  34. Phase Behavior of Mixtures - 9
    22 min
  35. Partial Molar Properties 1
    8 min
  36. Partial Molar Properties 2
    12 min
  37. Partial Molar Properties 3
    18 min
  38. Using Partial Molar Volume Problem
    7 min
  39. Example Problem Determining Volume of Pure Components to Mix
    16 min
  40. Partial Molar Properties 4 - Gibbs/Duhem Equation
    15 min
  41. Example Application of Gibbs/Duhem Equation 1
    17 min
  42. Computing Partial Molar Properties for Binary Mixtures
    16 min
  43. Expressions for Partial Molar Properties in Binary Mixtures
    20 min
  44. Computing Partial Molar Properties of a Binary System Example
    17 min
  45. Example Calculating Partial Molar Properties in Binary Mixture
    32 min
  46. Properties of Mixing
    26 min
  47. Properties of Mixing of Ideal Gases Part 1
    10 min
  48. Properties of Mixing of Ideal Gases Part 2
    15 min
  49. Properties of Mixing of Ideal Gases Part 3
    18 min
  50. Property Changes of Ideal Gas Mixtures Example
    10 min
  51. Example Calculating Change in Entropy for a Binary Mixture
    27 min
  52. Theory of Vapor/Liquid Equilibrium - 1: Chemical Equilibrium in Mixtures
    8 min
  53. Theory of Vapor/Liquid Equilibrium - Part 2 Gibbs Phase Rule
    8 min
  54. Gibbs Phase Rule
    8 min
  55. Theory of Vapor/Liquid Equilibrium - 3: Notes on Chemical Potential
    6 min
  56. Fugacity in Mixtures 1
    24 min
  57. Example Computing Fugacity of Pure Substance
    20 min
  58. Theory of Vapor/Liquid Equilibrium - Part 4: Cubic Equations of State for Mixtures
    9 min
  59. Fugacity in Mixtures 2
    25 min
  60. Example on Fugacity and Phase Equilibrium in a Binary System 1
    18 min
  61. Example on Fugacity and Phase Equilibrium in a Binary System 2
    28 min
  62. Example on Fugacity and Phase Equilibrium in a Binary System 3
    14 min
  63. Predicting Enthalpy of Mixing using the SRK and PR EoS
    42 min
  64. Where we've been and where we are going
    39 min
  65. Ideality in Solution
    0 min
  66. Fugacity in Ideal Solutions
    19 min
  67. Raoult's Law
    11 min
  68. Raoult's Law for a Binary System Example 1
    17 min
  69. Raoult's Law for a Binary System Example 2
    13 min
  70. Raoult's Law for a Binary System Example 3
    35 min
  71. Raoult's Law for a Binary System Example 4
    11 min
  72. Raoult's Law for a Ternary System Example
    22 min
  73. Binary Vapor/Liquid Equilibrium Using Fugacity Coefficients Example
    6 min
  74. xy for a Binary System using Raoult's Law Example
    10 min
  75. Ideal Solubility
    23 min
  76. Non-condenseable Component
    25 min
  77. Non-condenseable Component Example 1
    18 min
  78. Non-condenseable Component Example 2
    18 min
  79. Raoults Law (Pxy)
    30 min
  80. Raoults Law (Txy)
    22 min
  81. Ideal Solution Review
    21 min
  82. Excess Properties 1
    14 min
  83. Excess Properties 2
    25 min
  84. Heat Effects of Mixing
    11 min
  85. Activity Coefficients- Where We've Been and Where We're Going
    23 min
  86. Activity coefficient and Activity
    22 min
  87. Activity coefficients and VLE - 1
    11 min
  88. Activity coefficients and VLE Part 2
    11 min
  89. Activity coefficients and VLE - 3
    21 min
  90. Introduction to Excess Gibbs Free Energy Models
    75 min
  91. Analytic Expressions for Activity Coefficients from Excess Gibbs Free Energy
    17 min
  92. Modified Raoult's Law Pxy Example 1
    14 min
  93. Modified Raoult's Law Pxy Example 2
    14 min
  94. Modified Raoult's Law Pxy Example 3
    10 min
  95. Modified Raoult's Law Pxy Example 4
    18 min
  96. Excess Enthalpy Example 1
    29 min

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Questions and Answers

A: The trap sits at the order of 10^2 Pa/m. Plugging into the viscous Ergun term gives ΔP/L = 150(1−ε)^2 μ v / (ε^3 dp^2). Using ε=0.4 and dp=0.006 m lands near 90 Pa/m. Many engineers jump to inertial dominance or mix density into the viscous term.

A: The key threshold is the simultaneous ΔP rise and temperature noise. Tube-side fouling increases hydraulic resistance and destabilizes heat transfer. Air binding doesn't raise tube ΔP, and valve stiction wouldn't explain the steady pressure increase.

A: The hard part is volume flow. 25 kmol/h at 373 K is roughly 0.19 m³/s. At 0.7 m/s allowable velocity, area is ~0.27 m², giving a diameter near 0.5 m. Oversizing usually comes from mixing liquid properties into vapor sizing.

A: The boundary here is laminar versus transitional. Re = ρvD/μ gives about 560, well within laminar flow. Most mistakes come from slipping a decimal in viscosity or diameter.