Chapter 1 present prestige and Outlook for electrical energy offer and Its expense (pages 205–214): Richard P. Braatz
Chapter 2 a brand new examine power offer (pages 215–221): Riad N. Yammine
Chapter three The gasoline offer Outlook for business 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 by means of Raw?Material Use (pages 258–269): H. R. Carroll and James J. Angelo
Chapter 7 Experimental overview 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 superior Melter?Temperature keep an eye on (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 assessment of the Dual?Glass?Depth Melting proposal (pages 340–345): C. Philip Ross

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Extra info for Proceedings of the 43rd Conference on Glass Problems: Ceramic Engineering and Science Proceedings, Volume 4, Issue 3/4

Example text

Fig. 4. Briqueter compacting rolls. 24 1 Fig. 5. Briqueter feed to batch wagon. Fig. 6. Briquets drying in a batch wagon 242 Fig. 7 . Screw chargers feeding briquets. Fig. 8. Briquets entering the furnace. 243 Fig. 9. Briquet-roll wear. Fig. 10. Special hard-surface coating on roll segment. 244 Fig. 11. Briquets moving toward the bridgewall. 100 800 95 700 90 760 85 740 80 720 75 700 70 680 x- 65 660 LL 60 640 55 620 x v) 2 - 3 a . - $ z m 50 I I I 1 I 20 40 60 80 100 600 1: DAYS Fig. 12. 9 tonne; 1000 ft3/d = 30 m3/d).

Batch was sent to the former’s plant and compacted on a small, single-pocket briqueter. On completion of the trials in Chicago a production-size machine was rented and installed at Bucyrus. Figure 2 shows the machine in place in the basement below the mixing-screw outlet. The briqueter is rated for 3 tonnes/h (3 tons/h). The wetted batch flows into a feed hopper located above the briqueter (Fig. 3). The feed hopper has a revolving screw with a scraper blade attached. The action of the scraper and screw forces the wetted batch onto the compacting rolls.

However, the cold dampering air created other operating problems. Because the dampering air being introduced into the 650°C (1200°F) gas stream was only 66°C ( 150"F), volatiles would condense out and adhere to the surface of the top cone and physically restrict the flow of the exhaust. This would eventually cause the melter pressure to increase so that it was out of range of control by the dampering-air system. It was then necessary to physically remove the condensate buildup by hammering and scraping.

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