Abstract: The invention relates to a method for the controlled operation of an industrial oven which is heated in a regenerative manner and which comprises an oven chamber, in particular a melting tank, in particular for glass, having the following steps: injecting fuel into the oven chamber via at least one fuel injector, which is designed to inject fuel, practically without combustion air in particular, conducting combustion air to the oven chamber in a first period duration and conducting exhaust gas (AG) out of the oven chamber in a second period duration separately from the fuel in a periodically alternating manner by means of a left regenerator and right regenerator which are associated with the at least one fuel injector and which are designed to regeneratively store heat from the exhaust gas and transmit heat to the combustion air. A supply of the combustion air is automatically controlled by means of a control loop.
Type:
Application
Filed:
September 21, 2011
Publication date:
January 9, 2014
Applicant:
SOFTWARE & TECHNOLOGIE GLAS GMBH (STG)
Inventors:
Peter Hemmann, Andreas Birle, Thomas Schulz, Helmut Heelemann
Abstract: The present invention relates to regenerative thermal or catalytic oxidizers and methods of operation thereof for oxidizing combustible components of feed gas mixtures. In accordance with the disclosed invention, operation of the heater used to supply supplemental heat to regenerative heat transfer oxidizers is controlled such that the input load to the heater is varied between a maximum input load and a nominal input load in response to a measured control temperature. The present invention provides improved temperature uniformity across the system for more efficient operation.
Type:
Grant
Filed:
February 2, 2000
Date of Patent:
July 17, 2001
Assignee:
Monsanto Company
Inventors:
Yurii S. Matros, Grigori A. Bunimovich, Christopher A. Roach
Abstract: A regenerative heat exchanger system includes a heat accumulator provided in an insulating vessel for accumulating heat energy, the heat accumulator having a first end and a second end opposing to the first end and being capable of permitting gas to flow through a body between the first and second ends, a heating device for heating the heat accumulator in such a manner that the heat accumulator is formed with a plurality of temperature-different regions, a medium gas-supplying device for flowing medium gas through the plurality of temperature-different regions independently from one another.
Type:
Grant
Filed:
May 31, 1994
Date of Patent:
May 30, 1995
Assignee:
Fluidyne Engineering Corporation
Inventors:
Steven D. Hickel, Lynn C. Marksberry, Toshikazu Yamamura, Shuuhei Natani, Toshio Kurosaka
Abstract: The operation of a battery of coke ovens with regenerative change of draught on heating flues includes adjustably controlling the combustion of gases in the heating flues to insure uniform vertical heating of the coking coal in the coke oven chambers. Control elements for the operation of discrete heating flues in each heating wall are adjusted to insure uniform heating of the coking coal along the length of the heating walls. A gas supply rate is selected for the delivery of gas into the heating flues to define a carbonizing time corresponding to a high output capacity of coke from the coke oven battery. The heat consumption by the coking coal in the coke oven chambers is reduced during each regenerative half period by interruptions to the supply of gas at the gas supply rate without modifying or adjusting the control elements employed to insure uniform heat distribution in the heating flues.
Abstract: An industrial heating furnace wherein hot exhaust gases from the furnace are heat exchanged in a rotary ceramic heat exchanger with air which is supplied to burners in the furnace for combustion air. The temperature of the gases within the furnace is controlled and the ratio of the flow of gases through the two sides of the rotary heat exchanger is controlled at a predetermined value which is approximately one to maximize efficiency of the furnace operation and to minimize thermal stresses on the ceramic heat exchanger.