LearnChemE
LearnChemE
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Reversible Reaction in an Adiabatic Plug Flow Reactor (Interactive Simulation)
Organized by textbook: learncheme.com/ Demonstrates how to use an interactive simulation that demonstrates equilibrium for a reversible reaction in an adiabatic plug flow reactor. The simulation is located at: learncheme.com/simulations/kinetics-reactor-design/reversible-reaction-in-an-adiabatic-pfr/
Made by faculty at the University of Colorado Boulder, Department of Chemical & Biological Engineering.
Check out our Thermodynamics playlists: ua-cam.com/users/LearnChemEplaylists?shelf_id=11&view=50&sort=dd
Check out our Kinetics/Reactor Design playlists: ua-cam.com/users/LearnChemEplaylists?view=50&flow=list&shelf_id=7
Check out our website for interactive simulations: www.learncheme.com/simulations
Переглядів: 156

Відео

Immiscible Liquids on a Pressure-Composition Diagram (Interactive Simulation)
Переглядів 824 години тому
Organized by textbook: learncheme.com/ Demonstrates how to use an interactive simulation that plots the phase diagram (pressure versus mole fraction) for two immiscible liquids (benzene and water) . The simulation is located at: learncheme.com/simulations/thermodynamics/thermo-2/immiscible-liquids-on-pxy-diagram/ Made by faculty at the University of Colorado Boulder, Department of Chemical & Bi...
Henry's Law for Gases Dissolved in Water (Interactive Simulation)
Переглядів 884 години тому
Organized by textbook: learncheme.com/ Demonstrates how to use an interactive simulation that calculates the mole fractions of gas adsorbed in water as a function of temperature and pressure. The simulation is located at: learncheme.com/simulations/thermodynamics/thermo-2/henry-s-law-for-gases-dissolved-in-water/ Made by faculty at the University of Colorado Boulder, Department of Chemical & Bi...
Partially-Miscible Liquids (Interactive Simulation)
Переглядів 1074 години тому
Organized by textbook: learncheme.com/ Demonstrates how to use an interactive simulation that demonstrates the behavior of a binary liquid mixture that exhibits phase separation as a function of temperature. The simulation is located at: learncheme.com/simulations/thermodynamics/thermo-2/partially-miscible-liquids/ Made by faculty at the University of Colorado Boulder, Department of Chemical & ...
Enzyme Inhibition Kinetics (Interactive Simulation)
Переглядів 634 години тому
Organized by textbook: learncheme.com/ Describes how to use an interactive simulation that demonstrates the effects of inhibitor concentration on substrate consumption in enzyme kinetics. Three types of inhibition plus selectivity-inhibition can be selected. Lineweaver-Burk linearized plots are shown. This simulation is located at: learncheme.com/simulations/kinetics-reactor-design/enzyme-inhib...
Evaporative Cooling of Water (Interactive Simulation)
Переглядів 2354 години тому
Organized by textbook: learncheme.com/ Demonstrates how to use an interactive simulation that demonstrates evaporative cooling when water is evaporated from an adiabatic tank using a vacuum pump. The simulation is located at: learncheme.com/simulations/thermodynamics/thermo-1/evaporative-cooling-of-water/ Made by faculty at the University of Colorado Boulder, Department of Chemical & Biological...
Energy Balance in Open and Closed Systems
Переглядів 1304 години тому
Organized by textbook: learncheme.com/ Gives the energy balance for both open and closed systems and compares the two. Made by faculty at the University of Colorado Boulder, Department of Chemical & Biological Engineering. Check out our Material and Energy Balances playlists: ua-cam.com/users/LearnChemEplaylists?view=50&sort=dd&shelf_id=8 Check out our website for screencasts organized by textb...
Single Stage Batch Distillation Example Part 2
Переглядів 1154 години тому
Organized by textbook: learncheme.com/ Demonstrates using an Excel spreadsheet to solve the Rayleigh equation for a single-stage batch distillation in order to determine the amount of distillate that has a desired concentration of the more-volatile component. Made by faculty at the University of Colorado Boulder, Department of Chemical & Biological Engineering. See introduction screencast here:...
Addition Polymerization in CSTR: Spreadsheet
Переглядів 38021 день тому
Organized by textbook: learncheme.com/ Describe how to use a spreadsheet that calculates the concentration of polymer chains in a CSTR for addition polymerization without termination. The spreadsheet is located at learncheme.com/student-resources/excel-files/ Screencasts for the Polymerization of a CSTR, Parts 1, 2, and 3 are located here: ua-cam.com/video/ud_5fYsk67s/v-deo.html, ua-cam.com/vid...
Lineweaver-Burke plots for Michaelis Menten Enzyme Kinetics
Переглядів 340Місяць тому
Organized by textbook: learncheme.com/ Shows how the Lineweaver-Burke linear plots for Michaelis-Menten kinetics change for different types of inhibition. Made by faculty at the University of Colorado Boulder, Department of Chemical & Biological Engineering. Check out our Kinetics playlists: www.youtube.com/@LearnChemE/playlists?view=50&sort=dd&shelf_id=7 Are you using a textbook? Check out our...
Thiele Modulus Particle Size Effects (Interactive)
Переглядів 311Місяць тому
Organized by textbook: learncheme.com/ Estimates the effect of effective rate of reaction when the pellet size of a catalyst particle is increased for operation in a differential reactor. Made by faculty at the University of Colorado Boulder, Department of Chemical & Biological Engineering. Check out our Kinetics/Reactor Design playlists: ua-cam.com/users/LearnChemEplaylists?view=50&flow=list&s...
CSTR Material Balance: Effect of Increasing Volume on Yield (Interactive)
Переглядів 347Місяць тому
Organized by textbook: learncheme.com/ An interactive screencast exploring how a change in reactor size translates to a change in yield. Made by faculty at the University of Colorado Boulder, Department of Chemical & Biological Engineering. Check out our Kinetics/Reactor Design playlists: ua-cam.com/users/LearnChemEplaylists?view=50&flow=list&shelf_id=7
Two Reactions in a Two Phase Reactor
Переглядів 640Місяць тому
Organized by textbook: learncheme.com/ Based on outlet compositions, determine the flow rates and the selectivity for a two reaction system. Made by faculty at the University of Colorado Boulder Department of Chemical and Biological Engineering. Reviewed by faculty from other academic institutions. Check out our Material & Energy Balances playlists: ua-cam.com/users/LearnChemEplaylists?view=50&...
Systems of Units
Переглядів 3232 місяці тому
Organized by textbook: learncheme.com/ Compares SI and American units. Discusses base units and derived units. Made by faculty at the University of Colorado Boulder, Department of Chemical & Biological Engineering. Check out our Material & Energy Balances playlists: ua-cam.com/users/LearnChemEplaylists?view=50&flow=list&shelf_id=8 Check out our website for interactive simulations: www.learnchem...
Temperature Scales
Переглядів 2822 місяці тому
Organized by textbook: learncheme.com/ Describes the different temperature scales. Made by faculty at the University of Colorado Boulder, Department of Chemical & Biological Engineering. Check out our Material and Energy Balances playlists: ua-cam.com/users/LearnChemEplaylists?view=50&sort=dd&shelf_id=8 Check out our website for screencasts organized by textbook: www.learncheme.com/screencasts/...
Using Extent of Reaction for Multiple Reactions
Переглядів 3582 місяці тому
Using Extent of Reaction for Multiple Reactions
Chain-Growth Polymerization
Переглядів 4163 місяці тому
Chain-Growth Polymerization
Step-Growth Polymerization
Переглядів 2633 місяці тому
Step-Growth Polymerization
Solve Set of Nonlinear Equations Using Solver
Переглядів 5493 місяці тому
Solve Set of Nonlinear Equations Using Solver
Self-Study Module for Enzyme Kinetics
Переглядів 2243 місяці тому
Self-Study Module for Enzyme Kinetics
Linde Liquefaction Cycle on P-H and T-S Diagrams
Переглядів 5903 місяці тому
Linde Liquefaction Cycle on P-H and T-S Diagrams
Energy Balance on Tank with Steam Feed Part 2
Переглядів 4213 місяці тому
Energy Balance on Tank with Steam Feed Part 2
Conservation of Mass Example 2
Переглядів 3283 місяці тому
Conservation of Mass Example 2
Calculate Compressor Work Required to Form 1 kg of Liquid N2 in Linde Liquefaction
Переглядів 6063 місяці тому
Calculate Compressor Work Required to Form 1 kg of Liquid N2 in Linde Liquefaction
Calculate Liquid N2 Yield in Linde Liquefaction
Переглядів 4203 місяці тому
Calculate Liquid N2 Yield in Linde Liquefaction
Description of Linde Liquefaction Cycle
Переглядів 4593 місяці тому
Description of Linde Liquefaction Cycle
How Accurate is the Shortcut Van't Hoff Method for Chemical Equilibrium?
Переглядів 5133 місяці тому
How Accurate is the Shortcut Van't Hoff Method for Chemical Equilibrium?
Calculate NH3 Formation Equilibrium using Gibbs Minimization Spreadsheet
Переглядів 3673 місяці тому
Calculate NH3 Formation Equilibrium using Gibbs Minimization Spreadsheet
Why Does Salt Lower the Temperature for Making Ice Cream?
Переглядів 5153 місяці тому
Why Does Salt Lower the Temperature for Making Ice Cream?
Venturi Meter (Interactive Simulation)
Переглядів 7068 місяців тому
Venturi Meter (Interactive Simulation)

КОМЕНТАРІ

  • @kylecatman7738
    @kylecatman7738 День тому

    It's Qa - Wa = Qb - Wb not Q + W

  • @kylecatman7738
    @kylecatman7738 День тому

    Every textbook has U = Q - W

  • @kylecatman7738
    @kylecatman7738 День тому

    How is water a vapor at 80 C and 2 bar?

  • @whitenoisemachine6793
    @whitenoisemachine6793 День тому

    How do i do this with Moles instead of gram Though?

  • @foxhound1008
    @foxhound1008 2 дні тому

    In the last example, on the Enthalpy change, the enthalpy change is only equal to the heat added, as a liquid is incompressible. If the fluid was a compressible gas, wouldn’t we have to account for the PV work (flow work) done also? Or, because the pressure change is zero, there is no PV work?

  • @byw8396
    @byw8396 2 дні тому

    👍🏻

  • @assiopio9025
    @assiopio9025 3 дні тому

    Very cryptic. Altough I am still learning the disciplines on ChemeE course day by day, I'm still very disapointed for not having a natural comprehension of the topics my classmates seem to understantand - at least conceptually - so easily.

  • @franciscopagano99
    @franciscopagano99 3 дні тому

    where can i downlond this biotech software? Im trying to do a probabilty plot in excel but not succeding

  • @panagiotisathanasiou7918
    @panagiotisathanasiou7918 4 дні тому

    I guess you copy fogler without understanding what is going on. I am Disappointed. What is your Tref? Stop copy paste what ever you see in books.

  • @SnenhlanhlaZinhlekhumalo
    @SnenhlanhlaZinhlekhumalo 4 дні тому

    why we didint include that 70mol when we were doing overall balance

  • @panagiotisathanasiou7918
    @panagiotisathanasiou7918 4 дні тому

    Be serious ξ is called ksi

  • @r.santhosh1791
    @r.santhosh1791 4 дні тому

    I felt trouble in this concept before but now its clear thanks to you

  • @Galileosays
    @Galileosays 7 днів тому

    For an ideal system, this diagram is okay. In practice, one needs to consider the heat transfer coefficient of heat going in and heat going out of the heat pump per time unit. This transfer is temperature difference dependent. For instance, the compressed gas is adiabatically expanded to a temperature below the outdoor temperature. For fast flow at least 10 C below the outdoor temperature. Subsequently the cold expanded gas is heated by the outdoor temperature. Next the gas is compressed to a temperature above the room temperature. Subsequently the temperature drops to the desired room temperature. For efficient fast heat transfer the gas has to compressed to at leat 25 degrees above room temperature. The compressed gas releases the heat to the room to 5 degrees above room temperature. Say room is at T=293 K one needs Th=323 K. Say outside is T=283 K, then the compressed gas of 298 K should expand to 273 K. This gives Qh/W=Th/(Th-Tc)=318/(318-273)=6.

  • @kylecatman7738
    @kylecatman7738 7 днів тому

    he said if P2 = P1 then enthalpy doesn't change, but enthalpy is based on temp not pressure

  • @kylecatman7738
    @kylecatman7738 7 днів тому

    Work done ON a gas is negative, work done BY a gas is positive, correct?

  • @nurinsyamimi.
    @nurinsyamimi. 8 днів тому

    can COSMO-RS do this?

  • @lesedimabula7536
    @lesedimabula7536 8 днів тому

    How is m3 half the flowrate of m1?

  • @ryesbagh5210
    @ryesbagh5210 10 днів тому

    which programm did you use on deriester chart to help you and give you values of k ??

  • @mukonank783
    @mukonank783 11 днів тому

    Ooh yeah, I actually watched this video while I was still at school but now that I’m working I fully understand every small detail of each word you said. When I was still at school I noticed I didn’t really pay attention or fully understood the importance of 60% of the video

  • @RiccardoF
    @RiccardoF 11 днів тому

    great video

  • @yienannchoo82
    @yienannchoo82 12 днів тому

    Good morning/afternoon/evening. Regarding the mole fraction of component 1, x1, at 5:28, should we use the x1 in Alpha phase or the x1 in Beta phase?

  • @nathancoleman8648
    @nathancoleman8648 14 днів тому

    how is the temperature of the saturated steam the same as the condensed water? Isn't this essientially a heat exchanger, therefore the heat from the steam exchanges into the green solution meaning the condensed water would be at a lower temperature?

  • @chunhochan7174
    @chunhochan7174 14 днів тому

    May I know what are the remaining elements in the matrix other than the diagonal? i.e. C01, C02, etc. Thanks.

  • @musiconly7447
    @musiconly7447 16 днів тому

    what is the reason for the 1/3 exponent?

  • @TheKevinFanClub526
    @TheKevinFanClub526 20 днів тому

    04:20 "So we have a 3.3 molar solution of NaOH, so we need a 3.3 molar solution of HCL to neutralize the stream." It's the mole flowrate of the HCL that needs to match the mole flowrate of NaOH, not the concentration.

  • @Betty-z4Betty__505l
    @Betty-z4Betty__505l 20 днів тому

    By the whims of a system error, the transaction was sent to an invalid email address.

  • @serenade8905
    @serenade8905 21 день тому

    thank you, that's actually so helpful to understand the key concepts in each cell

  • @rarestudor5173
    @rarestudor5173 23 дні тому

    thank you so much!!

  • @VanessaDaz
    @VanessaDaz 26 днів тому

    Hi, I tried using this simulation. And I wonder if I can change the feed rate and quality? What if the feed that I want not 50% methanol and 50% water? Thank you in advance

  • @sitanshunaik6157
    @sitanshunaik6157 26 днів тому

    Thank you so much . Iam a NEET UG aspirant from India. And I was stuck in this concept and I was confused badly by mixed answers from various sites . Your one video cleared all confusions. Thank you sir❤

  • @kylecatman7738
    @kylecatman7738 29 днів тому

    Its Ti - Te and here that's a positive number same as the Work term being positive, fyi

  • @kylecatman7738
    @kylecatman7738 29 днів тому

    work out of the system is positive, the opposite of Q out of the system which is negative.

  • @rondavidjoseph7965
    @rondavidjoseph7965 Місяць тому

    How do you find delta h1 and delta h3

  • @kidpeanut
    @kidpeanut Місяць тому

    can you make for h2o2 beacoming h2o and o2?

  • @umizaharah4492
    @umizaharah4492 Місяць тому

    what is the question fpr this problem? i mean in words of paragraph?

  • @SaeedAmiri70
    @SaeedAmiri70 Місяць тому

    What's the reason for changing curve concavity by changing fluid? Does it depend on varying K or Cp values by temperature along the heat exchanger?

  • @kylecatman7738
    @kylecatman7738 Місяць тому

    I DO NOT agree that there is no work in this problem, the volume is increasing 4 fold for christ sakes!! Plus, the piston is being moved for crying out loud!! Total Bull on this one Falconer!!!

  • @rckygrhm1
    @rckygrhm1 Місяць тому

    Awesome! a very clear explination.

  • @muhammadshehreyarkhan1851
    @muhammadshehreyarkhan1851 Місяць тому

    I guess this formula is for UA clean & in case of UA dirty we have to add the fouling factor contributions on the inner & outer of the surface as well. What is the equation for that? Will the fouling factors be assumed from literature or calculated?

  • @muhammadshehreyarkhan1851
    @muhammadshehreyarkhan1851 Місяць тому

    Indeed a picture is worth thousand words.

  • @muhammadshehreyarkhan1851
    @muhammadshehreyarkhan1851 Місяць тому

    Thanks for the explanation in detail. In case of the reboiler using heat transfer fluid other steam which does not change phase i.e. hot oil, will the heat transfer coefficient of the reboiler be the same as that of the condenser?

  • @miguelangelcandeno4996
    @miguelangelcandeno4996 Місяць тому

    Using userform with checkbox in WORD?

  • @mirzasalkic5252
    @mirzasalkic5252 Місяць тому

    Could you explain why in the eq 7 there is + in front of the x1*W, when I found its originally - there

  • @RD-ud3eh
    @RD-ud3eh Місяць тому

    1:02 I have been unable to put/spin the turbun onto my head using this system, any ideas?

  • @omarhafiz5996
    @omarhafiz5996 Місяць тому

    So helpful, thanks

  • @jonathanstraiton4601
    @jonathanstraiton4601 Місяць тому

    Why is there a coefficient of "2" in the mass balance for A? I thought that was already accounted for with the Ca^2

  • @tanyilun2990
    @tanyilun2990 Місяць тому

    May I know which simulator are you using?

  • @marysherry7625
    @marysherry7625 Місяць тому

    What is x? And what is the purpose of solving x=0.91?

  • @CalebDietrich
    @CalebDietrich Місяць тому

    You multiply the H values (BTU per lb) by the total pounds of each stream in your energy balance. Are the units of H in "BTU per lb of total mixture" or "BTU per lb of H2SO4"? If you think about it, the enthalpy of mixing arises from mixing the H2SO4, not the other stuff in solution (which should be arbitrary to the total heat). So accounting for only the masses of H2SO4 from in and out of the mixer in the energy balance makes most sense to me. Is this logic flawed?