By David Lorge Parnas (auth.), Mehdi Jazayeri, Helmut Schauer (eds.)
This publication constitutes the refereed complaints of the sixth ecu convention on software program Engineering, FSE '97, held together with the fifth ACM SIGSOFT Symposium at the Foundations of software program Engineering, FSE '97 in Zurich, Switzerland in September 1997.
The quantity offers 27 revised complete papers chosen from a complete of 194 submissions. additionally integrated are six invited shows. All in all of the quantity is a different presentation of state of the art study and improvement in software program engineering. The papers are prepared in topical sections on software program engineering schooling, software program structure, methods, configuration and strategy instruments, formal research, empirical stories, procedure modelling, trying out, software research, and decomposition and distribution.
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Additional info for Software Engineering — ESEC/FSE'97: 6th European Software Engineering Conference Held Jointly with the 5th ACM SIGSOFT Symposium on the Foundations of Software Engineering Zurich, Switzerland, September 22–25, 1997 Proceedings
Gas turbine 6. duct burner 7. ammonia grid 8. SCR or CO catalyst 9. stack Figure 17-a & b. Arrangement of catalysts for NOx and CO reduction. before it reaches the catalyst, where the NO x is converted to N2 and H20. The excess of ammonia called ammonia slip should be minimized by proper controls. Base metal catalysts are suitable for higher temperature operation in exhaust gas streams containing higher levels of 50 x' In oil fired HRSGs the excess ammonia can react with 503 to form ammonium sulfate which can deposit on surfaces at low temperatures and cause fouling and corrosion.
Various gas inlet and exit configurations are possible; for instance the gas can enter at the top and flow downwards or exit at the side. Insulated downcomersare located at the turning section. K SILENCER lf4TERTUBE BOILED. TJrQ PASS UNFIRED H~ Figure 1-7a. A two-pass unfired HRSG with superheater, evaporator and economizer. [courtesy ABeD Industries]. The casing is internally insulated with 4 to 5 inches of mineral fiber or insulation and is protected from the hot gas stream by a stainless steel or corten or carbon steel liner, which is designed to move or expand in the plane of the casing.
If distillate is used, fuel quantity is read off the same scale as 4,300 lb/hr. If natural gas is used, it is 76,000 scf/hr. Connect oxygen = 15 with Wg =530,000 and extend to cut Qmax scale at 465 MMBtu/hr. By working in reverse, T2 can be obtained if Qs is known. The oxygen depletion is obtained by proportion. 86%. BASIC PROGRAM COMPUTES FUEL INPUT, FIRING TEMPERATURE For accurate computations one may use the program presented below. Supplementary fuel firing of turbine exhaust gases is frequently utilized in combined cycle and cogeneration projects (Figure 1-13) to generate additional steam from heat recovery boilers.