I found a picture of the scale model here:
http://www.leclairerail.com/MiscSubjects.html
http://www.leclairerail.com/Additions-2 ... erLima.jpg
the "photo" of the C&O J3a and a brief discussion can be found in "Perfecting the American Steam Locomotive"
By J. Parker Lamb
scanned here:
http://i894.photobucket.com/albums/ac14 ... /COJ3a.jpg
It appears that the 'double part refers to the fact that the Belpaire squarish shape of the furnace roof is carried through into the barrel, both top and bottom, in a way to form a combustion chamber of roughly square cross section between the furnace proper and the rear tube sheet.
I believe the advantage claimed is that the Belpaire shape has more radiant heat absorption surface than a cylindrical shape in the same envelope. hence a higher steaming capacity for a given boiler size/weight.
As for your other question about flow measurement inside boilers, one method is to mount a number of threaded bushings in various locations , flush with the surface on the water side, and insert 'averaging pitot' flow elements. the deltaP between the two sides of the element is proportional to fluid velocity. since the dP is only a few inches of water the attached indicator can be a simple U-tube manometer. the elements can be very thin tubing in a faired sheath to minimize the device's impact on the flow ! they can be inserted to various depths and rotated to find direction of flow as well as velocity.
In a confined channel like a tube this can produce very accurate mass flow measurement. In less restricted geometries such as a water leg around a radiant furnace with arrays of staybolts and two phase flow, the problem would be very complex, but precision would probobly not be needed, so much as assurance of a certain minimum velocity under varying conditions.