Bro you are just awesome and i'am also chemical engineer and your explanation seems to be like experinced professional and not like college lecturer. Kindly explain in english and don't bother about anyone. You are really helping a lot. Continue your service.
Please give some information about code and standard for design aspects. I m 17yrs experience in design but whenever i see ur videos its always something new.
Your informative videos are highly beneficial for non chemical engineers like us working in the refining industry. Thank u for the well put in effort. A kind request: could u put up a video on the explanation of amine strength, its effect, kinds of ami e and their merits/demerits and associated knowledge in the industry!
Very good explanation. Thanks for such videos. Q1.when we see the P&ID psv set value remains the same for cases, even where multiple psv's are available. I haven't seen any case where one psv set value is set at 50 and other at 52.5kgf/cm2g. Just for information. Q2. As the MAWP/MAAP or lessthan the hydrotest pressure, does that mean we can run the vessel at high pressures above design for specific period of time? If so how much? Considering psv in isolated condition. Q3. How to calculate the burst pressure? Q4. From where do we find the MAWP values of different vessels in the process unit? Thabk
15.88 mm(OD) x 0.6mm thickness of copper tubes length 10 MTR IS 11329 clause no. 7.3.1 ke anusar disign pressure low side and Haiger side kitna hoga. Kindly update us.
Sir its too much confusing ,between psv and prv when u r relating with terms..pls add short vidio so its clear terms related to safty valve and relef valve..
Sir I have one doubt I have lecture notes and standard book but to get grip own concept i want to watch nptel lectures so did u take notes from nptel while u were preparing
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Bro you are just awesome and i'am also chemical engineer and your explanation seems to be like experinced professional and not like college lecturer. Kindly explain in english and don't bother about anyone. You are really helping a lot. Continue your service.
When I upload in English then I get so many comments for uploading in Hindi. I simply can not upload in 2 language because of time constraint.
Keep in Hindi sir. 👍
Highly informative from highly informed person....aap ki sath ho nothing is confusing at all....love you sir....
Sir I'm doing job, your vedios are very helpful for understanding real life concepts regarding static and rotating equipment,
Thank you sir 🙏
Please give some information about code and standard for design aspects.
I m 17yrs experience in design but whenever i see ur videos its always something new.
Thanks You So much sandip sir .❤
Your informative videos are highly beneficial for non chemical engineers like us working in the refining industry. Thank u for the well put in effort. A kind request: could u put up a video on the explanation of amine strength, its effect, kinds of ami e and their merits/demerits and associated knowledge in the industry!
Very good explanation. Thanks for such videos.
Q1.when we see the P&ID psv set value remains the same for cases, even where multiple psv's are available.
I haven't seen any case where one psv set value is set at 50 and other at 52.5kgf/cm2g.
Just for information.
Q2. As the MAWP/MAAP or lessthan the hydrotest pressure, does that mean we can run the vessel at high pressures above design for specific period of time? If so how much? Considering psv in isolated condition.
Q3. How to calculate the burst pressure?
Q4. From where do we find the MAWP values of different vessels in the process unit?
Thabk
Great Explanation. Thank you for the summarized information.
Please make a video on 3% pressure drop loss in psv inlet line.
Sir please make a video about the auxiliaries of a compressor and the common arrangement comprising of units like sunction kod, aop, rundown tank etc.
Rupture disk ke bare me kuchh bataiye sir.
Thank you so much sir 🙏
Can you please suggest me some books as i am preparing for boiler inspector and boe
Well explained. Thank you so much.
Very well explained
thank you sir, great explanation
If PSV set at design pressure in that case working pressure and MAWP are same whatever as per API 520 it is also valid for more volatile components
Great explanation
Once again very good informative video💐💐
Nicely explained 👌
Sir iske liye konsa book refer kiya apne?
Very nice
What book u have referrred for indian standard?
Nice efforts
15.88 mm(OD) x 0.6mm thickness of copper tubes length 10 MTR IS 11329 clause no. 7.3.1 ke anusar disign pressure low side and Haiger side kitna hoga. Kindly update us.
Very nice....Thank you
Sir its too much confusing ,between psv and prv when u r relating with terms..pls add short vidio so its clear terms related to safty valve and relef valve..
Sir I have one doubt I have lecture notes and standard book but to get grip own concept i want to watch nptel lectures so did u take notes from nptel while u were preparing
Yes, I used to make notes while watching nptel videos.
Which NPTEL course you Followed
Sir why blowdown occurs?
Rated pressure????
Hi.
Sir voice thoda kabhi kabhi slow ho jata hai...mic suitable nahi hai
koi aur aisa complain nahi kiya....batayie to kis time pe voice slow ho gaya hai ?
Mesh rm.
Mesram
Blowdown last pe samaj nehi aya
koi baat nahi....Next video will be on PSV. Everything will be clear in that video.