CONTINUOUS HEATING FURNACES
chamber by a port in the hearth of the furnace. The velocity
of the current of gases in the chamber is retarded because the
chamber is formed as an inverted weir having a reservoir (the
height of the roof above the hearth being hi>h); the ingots are
carried upon the hearth. Two currents of gases are possible:
aa immediately below the roof and bb over the hearth. In order
to reach the waste-gas outlet the hot gases aa must descend a
distance hi and expend in doing this a certain hydrostatic pressure,
which will be designated as 8 mm of water. The current bb has
to overcome the friction of the ingots. It is evident that the hot
gases cannot escape immediately through the waste-gas opening,
except in a case where the resistance to the passage of the current
of cooler gases bb, equal to <5i mm of water, is greater than 5,
that is to say, in a case where <5i is greater than 5.
The greater the width of the furnace in proportion to the
length of the ingots, the less will be the value of <5i; and therefore
there will be no reason to fear that the hot gases will pass imme-
diately to the waste-gas flue.
When the ingots are placed upon pipe skids (Figs. 119 and 120)
a channel pp will be formed below them through which the cooler
waste gases will flow to the waste-gas port q. The heating chamber
having a descending roof, a free space mm, a well-defined com-
bustion chamber, will be formed under this roof, providing a
rationally constructed heating chamber for continuous ingot
reheating furnaces. W
Figs. 119 and 120 show two methods by which the flow of the
reacting gases may be slowed down sufficiently to permit combus-
tion to be completed in the front portion of the heating chamber.
In Fig. 119 this is done by a sharp drop in the roof, dividing the
heating chamber into two sections, one much higher than the
(1) This arrangement, moreover, facilitates the operation of the furnace by
making it easier to roll the ingots over while they are heating.