Hello all.
Earlier posts by Vtsteam's on monotube theory is what drew me to this forum in the first place. It was an interesting read and obviously much thought went into it. Most of his design priorities are right in line with my own with safety being at the top of the list and efficiency bowing down before steady steaming tendencys. An off-the-shelf quality is my second priority right along side with using sched. 40 galvanised pipe and sched. 80 screw-together fittings. I should say at this point that the boiler I am designing for will operate within lower pressures of 10 to 40 p.s.i.g.
Many experts on boiler theory claim that monotube design is a very tricky and exacting process and there are legions of ways to go wrong. And that is why I am following a hair pin configuration, screw-together approach --- especially for a first boiler attempt. It makes experimentation and re routing of tubes very convienient. It also makes repair of burnt tubes a matter solveable by a pipe wrench.
If impingement of gases upon pipe threads is a concern, then solutions of wrapping the fittings with insulation are easily doable. Contriving some kind metal type walled barrier is a design complication but also do-able.
I would indeed like to come upon a list describing the reasons for given design failures, but have not come across such yet. If any reader knows of a source please shoot it my way. I imagine the predominent issues are water sluggung, water hammer, and inability to estabilish or maintain a stable transition zone. I do believe that most of the bugaboo about monotubes comes from those using them in the highly variable load demands of steam cars.
As mentioned in Vtsteam's post, it would seem diameter of tube for a given horsepower rating needs to be nailed down pretty tight. Surely turbulant flow must be obtained for good steambubble scrubbing, while at the same time trying to minimise pressure drop along the tube or tubes if multi-path is being used.
For me, the pipe diamiter has been predetermined by oppertunism as I was able to obtain bucket loads of 1/2" sched. 80 threaded pipe fittings at scrapyard prices....not exactly the scientific, technicalogical approach but "rather just going with the flow when the flow seems to be going in my general direction.
Vtsteam in his earlier Feburary post, pondered the use of flow vs counterflow to hopefully stabalize the transition zone. His suggestion of parrallel flow seems logical to me as the cooler tubes with their greater temp differential to the gases will more rapidly absorb heat and the hotter tubes would have a much lower differential resulting in less effecient heat absorbtion and higher flu gas temperatures. These higher exiting temps could simply be recovered with a larger economiser which would be a small price to pay for transition zone stablization.
Besides parrallel flow and counter flow there is also variations of the two. For example, devide the entire generation tube assembly into thirds and play around with different stacking combinations. Another possibility is to use both parrallel flow and counter flow together in different combinations.
One concern, however that may have to be concidered is shocking the tubes by pulsing water that is too cool through pipes located in the zone of hottest gasses. Again, a larger economiser could remedy that. This is one of the issues that I will have to be on my toes about as I will be using a " rocket stove" type set up to burn solid fuel . Such a firebox design achieves very high temperatures and a clean burn which will possibly eliiminate sooting problems altogether.
Another bennifit of a "rocket stove" technology is that it allows for the isolation of the firebox from the generating tubes --- safetywise a great advantage...but at a high price. I have read that radiant heat can be as high as 90% more effecient then convective heat. Just on a gut level, that seems high. What ever the effeciency trade off though, some of the loss can be made up with the higher heat of the gasses typically produced by rocket stoves, and maxamising the angle of impingement...and of cource more tube surface.