Content:
Chapter 1 present prestige and Outlook for electrical energy offer and Its fee (pages 205–214): Richard P. Braatz
Chapter 2 a brand new examine strength provide (pages 215–221): Riad N. Yammine
Chapter three The gasoline offer Outlook for commercial clients (pages 222–235): Daniel A. Dreyfus and Edward S. Tabb
Chapter four Batch Briqueting—A creation Trial (pages 236–246): James R. Brown
Chapter five Recuperators on Insulation?Glass Unit Melters (pages 247–257): Thomas F. Stark
Chapter 6 Energy?Efficiency development via Raw?Material Use (pages 258–269): H. R. Carroll and James J. Angelo
Chapter 7 Experimental evaluate of NOx keep watch over utilizing a Glass?Tank Simulator (pages 270–293): Hamid A. Abbasi, Mark J. Khinkis, Richard T. Waibel and William D. Boyd
Chapter eight usage of Infrared Thermometers to accomplish greater Melter?Temperature regulate (pages 294–304): Richard W. Marshall
Chapter nine Gas?Burner Firing Practices (pages 305–320): Glenn Neff
Chapter 10 the 1st crusade of a Cold?Top electrical Furnace (pages 321–339): Carl W. Hibscher and Richard C Carle
Chapter eleven Operational evaluate of the Dual?Glass?Depth Melting proposal (pages 340–345): C. Philip Ross
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4 :Actual. Projected. 'Excludes synthetic gas from petroleum and coal. 'bncludes hydroelectricity, imported electricity, geothermal, renewables, etc. Table 11. 1982 GRI Baseline Projection of U. S. 4 *Actual. 'Projected. 'Primarily losses in electrical generation and transmission and coal gasification. Table HI. 7 *Actual. 'Pro'ected. 'Incjudes renewables and direct geothermal heat. 228 Table IV. 8 ;Excludes industrial material and feedstock consumption of energy; figures are derived analytically.
Metering of the H 2 0 is affected by flow raters located above the screw. The screw speed is adjusted via a variable-speed drive at the outlet end. As the trial progressed the screw mixer developed the capacity of 5 tonnes/h (6 tons/h). However, 3 tonnes (3 tons) were sufficient for continuous operation. The H 2 0 and batch mixture is fed through the floor to the compacting machine located in the basement. Compacting and Feeding the Batch The method for compacting the batch was developed by the K.
As will be noted several times later in this discussion, a primary concern is the protection of the hot inner liner of the recuperator from excessively high temperatures and reducing conditions. It is the constant flow of cold combustion air through the recuperator that cools the inner liner, thus preventing overheating. Because this flow cannot be interrupted for any reason, be it blower failure or electrical power failure, the stand-by blower is gas-engine driven and is designed to start automatically on power failure or loss of inlet-air pressure to the recuperator.