Thank you for the lecture. What should be the unit of molecular weight of the gas in this calculation? Is it gram/mole?

Thank you, excellent explanation, I see you are calculating using theoretical stages, if I assume a tray efficienty of 0.5, that would be the double of trays right?

great

Does expansion valve of refrigerator follow flashing curve?

Tray tower Sizing kzfaq.info/get/bejne/hNinZ6mcuLalpZs.html

Where can i find the reference for the equations used?

Please share your email address

Great, learnt lot with simple understanding

i innstalled crack version but it showing licence,can you sharemore information on yournext video

Can anyone pls explai6me those charts and how to read / solve them ?

sir can you share this excel file

Very well explained, thank you!

This solved my confusion

A trayed tower operating at 1 atm is to be designed to continuously distill 200 kmol/h (55.6 mol/s) of a binary mixture of 60 mol% benzene, 40 mol% toluene. A liquid distillate and a liquid bottoms product of 95 mol% and 5 mol% benzene, respectively, are to be produced. Before entering the column, the feed-originally at 298 K-is flash-vaporized at 1 atm to produce an equimolar vapor liquid mixture (VF/p=L/p= 0.5). A reflux ratio 30% above the minimum is specified. Calculate: (a) The quantity of the products. b) The minimum number of theoretical stages. (c) The minimum reflux ratio. (d) The number of equilibriumn stages and the optimal location of the feed stage for the reflux ratio specified. Could you please solve this problem?

Excellent!!

what if we dont know the tube diameters in advance. We have to select some size from a table based on the optimal velocites and flow areas based on the given flow rates?

Can u share the pdf

Sir how do we know the max velocity

Good presentation-Mohan

How was the max velocity found ??

Excellent video. What about the elbows? Are they short radius or long radius? In my 42 years in the business, I’ve seen more hydronic inefficiencies due to the use of short radius elbows. It seems like most engineers just don’t get it.

Good

Nice

Thank you very much for this video. however i still have a question. How to obtain the operating volume flow using the standard volume flow when the medium is water vapour?

f0c4 742d 1b74 420b efdc b1c0 f4a8 c02e [email protected]

Why cant we take flows in Ltr/sec or Gal/sec? Why cant we keep it simple.

great video.. may I know which equation may I used for steam? Hope u reply me back. Thanks

Very very good video

I would think the SG value for the 20Deg C case should be higher than that of 98DegC case looking at the density temperature chart

real deal 🔥

my e-mail is [email protected]

cefe 752b 25e0 7763 21cb 1625 042b 8ba3

are these methods valid for power hydraulics valves too?

Can I get this excel sheet.

Useful video! this app helped me with sizing calculations! play.google.com/store/apps/details?id=com.hiottech.valveitfree

I would like to know if these steps would work in the case of a full factorial design or fractional factorial design

Many thanks for your video. I tried the same thing with 3 factors (two levels) with 8 experiments (full factorial 2^3 Design) yet the model values are the same as the response values. What does that mean?

Good is there a book where I can find all these equations?

Very nice presentation to understand about control valve.thank u

513e 7583 b270 2450 fd96 d327 4fe6 fd24 [email protected]

fc37 7567 6595 3fd3 9fe8 e806 fa7d 484b [email protected]

Simple use KG tower and aspen hysys 😂

I can't believe Seattle did not run the ball

061a 75a7 7275 fb2a 394c 226d 4b39 9f5c ([email protected])

good but how to find F l, liquid pres recovery factor

Thank you so much. You explained this excellently. God bless!!!!

02d5 7613 9e12 2786 1568 bc28 8b7a a0b5 [email protected]

65ca 76d5 125f e37e 92dc 20ef 8083 db6e [email protected] Thanks

thanks mister. Just a suggestion. please put up a pointer/cursor when you are talking about anything paticular in your slides. I got confused many times, had to spend 1 and a half hour for this

thanks for this video. its very clear. Could you share the presentation