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#1
Posted 19 February 2012 - 03:50 AM
#2
Posted 19 February 2012 - 06:35 AM
Let you try this resource : Boliers,Evaporators & Condensers by SADIK KAKAC
It may help
Breizh
#3
Posted 20 February 2012 - 12:31 PM
For your application of such high pressure and temperature a fire tube boiler may not be suitable. Refer the link below where a brief description of water tube boilers is provided:
http://en.citizendiu...Steam_generator
Also try to get hold of a book on steam generation which is condsidered the ultimate resource on steam generation using either fossil fuels or nuclear fuel. The book is:
"Steam, Its Generation & Use" by the Babcox & Wilcox Company
Regards,
Ankur.
#4
Posted 20 February 2012 - 06:48 PM
I have installed and employed a lot of these types of boilers and have found that the usual top steam pressure generated by this type is approximately 75 to 100 psig (5 to 7 barg). In some cases, I have heard of installations generating 150 psig (10 barg) steam. But certainly 82 barg and 520 oC (968 oF) is totally out of the question. If those are still your steam design conditions, then you must go into a water tube type boiler design. You have no option because of the limitations of the hoop stress placed on a fire tube boiler shell. The smaller the diameter, the larger the allowable pressure in a vessel. Therefore, this is the basic principle by which you arrive at a water tube boiler - since a pipe is the practically smallest vessel diameter that you can use.
The book that Ankur mentions is the classic published by Combustion Engineering, Inc. I got a free copy as a senior Chemical Engineering student in 1959. My copy was edited by Otto de Lorenzi; it was a First Editon, eleventh impression, and second printing at that time. I still have it in my library, but I don't think you find a copy unless you have considerable luck where you are at. I quote from the book, with regards to firetube boilers:
"This is one of the oldest types of firetube boilers. these boilers are built with a combination of welded and riveted construction only, and the design pressure is limited to 250 psig. The capacity range is from 1,000 to approximately 15,000 lb/hr of saturated steam." These boilers do not produce superheated steam.
Good luck.
#5
Posted 23 February 2012 - 01:01 PM
#6
Posted 28 February 2012 - 01:15 PM
i shall be very thankful to you..kindly provide me some of you more practical knowledge about water tube boiler because a far as i know when corrosive gases are involved then you prefer to shift them toward tubes, how to justify our use of water tube i this case.
#7
Posted 28 February 2012 - 01:27 PM
The book
"Steam, Its Generation & Use" can be ordered from the link provided below:
http://www.babcock.c...rary/steam.html
Regards,
Ankur
#8
Posted 28 February 2012 - 01:36 PM
Regards
Madiha
#9
Posted 28 February 2012 - 02:00 PM
i have read somwhere that as far as the problem of assigning the corrosive gasses towards the shell(water tube boiler) which is generally not preffered, this problem can be resolved by mounting the boiler vertically so that scaling and other depositions can be peventes..kindly comment on this point of view..
Regards,
Madiha
#10
Posted 28 February 2012 - 10:12 PM
Tell us WHERE, exactly, you heard that there is a problem with "the corrosive gases being on the shell side of a water tube boiler". It is important to know this because the claim is nonsensical and illogical - besides being an untruth.
If the combustion gases are corrosive, you will have a corrosion problem regardless whether the gases are on the "shell" side or the tube side. If that were the case, you simply apply corrosion resistant refractory coating on the "shell side" and employ high alloy (expensive) water tubes. The solution is that simple.
#11
Posted 01 March 2012 - 04:56 AM
I'm wondering if these rules also apply to the design of the Waste-Heat Recovery section of a Sulfur Burner.
I'm basically trying to design a sulfur burner, to produce 3 TPH of SO2.
I have questions as:
1. Because im producing SO2 for Sodium Bisulfite mfg, i have very low O2 and SO3 tolerance levels. How can i design the Burner for this?
(will the Lurgi two-stage burning help here?)
2. Also, i need to estimate the amount of steam that can be generated. How does one go about these calculations? what data will i require?
Thanks
pkamat
#12
Posted 01 March 2012 - 07:06 PM
What "rules" are you referring to? There haven't been any rules discussed in this thread up to now. What has been discussed is good, sound, experienced heat transfer design engineering - something that is started at the learning stage in university courses.
Sulfur burning and burners are conventional type of equipment in today's state of the art. You should have no problem doing research work in the internet for specific burner information.
You generate sulfur combustion calculations in the normal, logical way that you have been taught as a student. This is a straight-forward combustion calculation routine and should be no problem. It involves basic stoichiometry and leads you directly to the amount of steam that can be generated. The data you require is the lower heating value of Sulfur, of course. This is pretty logical and basic.
If you want to find out more or have further questions on your Sulfur combustion problem, please start your own original thread in this Student Forum so that we don't hijack this thread away from its origninal poster (OP).
#13
Posted 02 March 2012 - 12:40 AM
Babcock and Wilcox Steam Reference
Breizh
#14
Posted 07 March 2012 - 06:31 AM
Thanks for the reply and i apologise for 'hijacking' this thread.
The "rules" i mentioned are the basic rules of thumb that you've provided in your former posts. I just wonder whether they apply to a sulfur burner.
I've performed all the basic combustion calcs...but I doubt the % excess (10) that i have used. There's nothing useful on the internet that i can find.
The same regarding the selectivity towards SO3 formation.
Thanks, really appreciate it
pkamat
#15
Posted 29 April 2012 - 09:15 AM
are the calculation for LMTD(log mean temperature for a waste heat boiler) is deifferent from simple exchanger due to phase cahnge?..
for my WHB the gases are on tube side with inlet pressure at 2 bar and temperature at 563 C while the oulet temperature is 325C,while BFW is entering at 126C & 84 bar while saturated steam is generated at 298 C & 83 bar...plz plz tell me for this case my tube sude heat transfer coefficient can be 0.6 W/m2 C,is it possible?
#16
Posted 29 April 2012 - 10:51 AM
Please refer the attachment as a guideline for calculating the heat transfer equation.
Regards,
Ankur
Attached Files
#17
Posted 29 April 2012 - 02:28 PM
Refer to this link and attachments, Hope this helps you.
http://www.steamline...la/history.html
http://www.me.ua.edu...ALS/Boilers.pdf
Regards
Shivshankar
Attached Files
Edited by Shivshankar, 30 April 2012 - 01:24 AM.
#18
Posted 01 May 2012 - 09:46 AM
The link you gave me was helpful in calculating tube side coefficient but not for shell side were boiling is taking place,kindly help me with it.i shal be very thankful to you.
#19
Posted 04 May 2012 - 03:29 AM
Here you can find both tube and shell side coefficient in below link,
http://www.cbu.edu/~rprice/lectures/stcalcs.html
Regards
Shivshankar
#20
Posted 13 May 2012 - 06:57 AM
please provide me the link for downloading Applied heat transfer by v.ganapathy.please
#21
Posted 13 May 2012 - 07:16 AM
Are you asking for a free download link for the book you have mentioned? You are not permitted to solicit free download links as per the rules of the forum. It is strictly prohibited. Please take a note of it.
Regards,
Ankur.
#22
Posted 13 May 2012 - 07:33 AM
#23
Posted 13 May 2012 - 07:42 AM
#24
Posted 13 May 2012 - 07:48 AM
thanx a million.plx help me members, i have my final year design presentation on boiler(fired tube type)..plx give some material from were i cal clear my concepts on boilers and heat transfer fundamentals.n different terms like critical heat flux, burnout point etc etc.
#25
Posted 13 May 2012 - 07:52 AM
Breizh
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