Automatic minimum differential pressure control for dryer...

F - Mech Eng,Light,Heat,Weapons – 26 – B

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122/30, 34/53

F26B 21/06 (2006.01) D21F 5/02 (2006.01)

Patent

CA 1249719

ABSTRACT OF THE DISCLOSURE A supply of steam is fed to a drying cylinder (10) from a steam line (20) through a steam pressure control valve (22). Condensate and steam are removed from the drying cylin- der to a separator (32). The pressure of the removed steam is controlled by a steam pressure control valve (36) and the rate of condensate removal is monitored by a condensate removal mon- itor (48). A computer controller (16) adjusts the steam feed and removal pressure control valves to maintain the smallest differential pressure therebetween which will maintain the con- densate removal rate substantially constant. The computer con- troller sets an initial pressure differential during an ini- tializing step (50). In a first pressure differential adjust- ment step (52), the computer decreases the pressured differen- tial in first increments until the condensate removal rate be- gins to decrease. In response to the decrease, the first pres- sure differential adjusting step increases the pressure differ- ential by the first increment. A second pressure differential adjusting step (54) functions like the first pressure differen- tial adjusting step but uses a smaller increment. A checking step (56) periodically increases the pressure differential by the second increment and returns the program to the second pressure differential adjusting step to reestablish an optimal pressure differential.

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