duncan webster | 21/11/2017 16:36:17 |
5307 forum posts 83 photos | I'm trying to find out where the L/d^2 rule of thumb for boiler tubes comes from, all references seem to point back to Mr CMKeiller. I've done a search and the relevant issues seem to be : 1934 issue 1755 1938 issues 1933, 1940, 1947 and 1955. Is there anyone out there who has copies this far back and would be kind enough to scan them for me? |
julian atkins | 21/11/2017 23:48:30 |
![]() 1285 forum posts 353 photos | Hi Duncan, I think you need to consider the SMEE Journals. C M Keiller was a SMEE member. He provided his formula to Martin Evans when Evans was writing his book on boiler making in the 1960s. Jim Ewins had his own views which were also published in the SMEE journals and also the Maidstone MES newsletters which have been archived. They are also in Evans' book. The fullsize formula is in Jos Koopmans' book 'The fire burns much brighter' available from Camden. I have always used generous tube diameters via length for both ordinary flues and superheater flues. Cheers, Julian
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Martin Johnson 1 | 22/11/2017 08:55:10 |
320 forum posts 1 photos | Hi Duncan, The first material in my collection were responses by Martin Evans and D.E. Lawrence to an article by E.C. Martin in the M.E. for March 19, 1971. The article by Evans gives some background to the Keiller tube factor; it seems this was derived by C.M. Keiller from correlation of the proportions of full size locomotive boilers. In addition, all the boilers "correlated" seemed to be express or mixed traffic standard gauge examples. (Choosing the data to suit the theory perhaps?) Keiller recommended a factor in the range 55 - 70, which many these days seem to think is a bit high - which rather ties in with Julain's comment "I have always used generous tube diameters via length for both ordinary flues and superheater flues." Keiller quoted work by Dr. Wagner of the German State Railways. Dr. Wagner had concluded that for maximum heat transfer, the gas flow area to heat transfer area should be around 0.0025, equivalent to L = 100 D - which has been called into question at the recent ASTT conference! Tubes of that length would certainly give good efficiency of the BOILER, but not necessarily of the whole loco. If you look at the Ewins boiler factor Eb = Grate Area in square inches x Tube Length in inches Number of tubes x (tube diameter in inches)² you will see it contains the Keiller factor. Ewins did a write up in EIM in the '80s but I don't have the reference by me just now. As you know, I happen to think that with the computing power we all have these days, we can do a lot better than these formulae. I am currently producing some worked examples starting with a "Speedy" boiler, which shows performance will be remarkably insensitive to changes in flue size - provided you keep roughly the same flow area. Things are a little more sensitive to flow area, but there is still plenty of leeway in practice. Hope that helps a bit Duncan. Martin |
Phil H1 | 22/11/2017 17:31:39 |
467 forum posts 60 photos | Martin, If you have discovered that there is plenty of leeway in flow area and the boiler is insensitive to changes in flue size - why do you feel that there is a need to do a lot better with computing power? Are there other areas of boiler design that you feel is in need of development? Phil H |
Clive Foster | 22/11/2017 18:07:27 |
3630 forum posts 128 photos | Lot of leeway and insensitivity to change means either :- 1) the system really is insensitive 2) everything is well off optimum so messing around with one parameter doesn't do much, basically lots more ways of being half right than dead right. 3) the system is self regulating over a useful range so varying one parameter sets off compensatory changes in other parameters. Good luck with sorting that out on an ordinary digital computer. Job for hybrid digital and analog one but they are bit our of fashion these days. 1 and 2 usually look the same but seriously aren't. Clive.
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duncan webster | 22/11/2017 18:34:55 |
5307 forum posts 83 photos | If Keiller's factor is based on full size then it probably has little relevance to models, as flow in full size tubes will be turbulent, and in models is laminar. I've always had an issue with Jim Ewins Eb factor as if you apply it to a large boiler Tich you come up with: grate area = 4.625 tube length = 4.25 Eb = 80 n*D^2 = 0.246. This suggests that 4 off 1/4" tubes would be OK, but this only gives tube area/ grate area of 4%, which just feels wrong. The Keiller factor for these tubes would be 69, well within range. A decent design guide should cater for a range of boiler sizes Julian says that he uses tubes shorter than Ewins/Keiller would suggest, and builds successful locos. Tubes saller or longer than needed for heat transfer need more smokebox vacuum, so more exhaust back pressure, so it matters. If Martin's work comes up with better design guides then it is well worthwhile. |
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