Thermal stack effect

As part of a Process Hazards Analysis (PHA). I was required to check a naturally ventilated building containing electrical equipment and a fuel gas supply, for adequate air flow due to thermal forces (stack effect). API RP 500 has a method that they recommend for buildings of l,000fP or less. The building in question was much larger, because ... 

To overcome thermal entry effects, the segments may be virtually stacked with the outlet conditions from one segment that becomes the inlet conditions for the next downstream section. In this approach, axial conduction cannot be included, as there is no mechanism for energy to transport from a downstream section back to an upstream section. Thus, this method is limited to reasonably high flow rates for which axial conduction is negligible compared to the convective flow of enthalpy. At the industrial flow rates simulated, it is a common practice to neglect axial conduction entirely. The objective, however, is not to simulate a longer section of bed, but to provide a developed inlet temperature profile to the test section. 

One of the most important aspects of 4-fluoro-6-methylbenzimidazole as a modified nucleobase is its strong stabilization of duplex DNA through a stacking effect. The stacking properties of 97 and other modified nucleosides can be measured by the dangling end thermal denaturation studies of DNA duplexes with self-complementary stands (dXCGC-... 

Lin, C.K., Huang, L.H., Chiang, L.K., and Chyou, Y.P. (2009) Thermal stress analysis of planar solid oxide fuel cell stacks effects of sealing design. J. Power Sources, 192, 515-524. 

In stacked reservoirs, such as those found in deltaic series, it is common to find that some zones are not drained effectively. Through-casing logs such as thermal neutron and gamma ray spectroscopy devices can be run to investigate whether any layers with original oil saturations remain. Such zones can be perforated to increase oil production at the expense of wetter wells. 

This section deals mainly with the interaction of thermal models as outlined in Section J 1.3 and airflow models as described in Section 11.4 for the purpose of integrated modeling of thermally induced (stack-driven) natural ventilation, governed by the thermal behavior of the building. For the integrated analysis ol air velocity fields and radiative and thermal effects in the building using CFD codes, see also Section 11.2 and Ott and Schild.-... 

A complete fuel cell system, even when operating on pure hydrogen, is quite complex because, like most engines, a fuel cell stack cannot produce power without functioning air, fuel, thermal, and electrical systems. Figure 3 illustrates the major elements of a complete system. It is important to understand that the sub-systems are not only critical from an operational standpoint, but also have a major effect on system economics since they account for the majority of the fuel cell system cost. 

Gas fuel contains more hydrogen than coal, thus giving rise to more water vapor in the boiler-stack gases and a relative reduction in thermal efficiency (enthalpy loss), due to the cooling effect of the water. 

As excess air is reduced, theoretical flame temperature increases. This has the effect of reducing the stack loss and increasing the thermal efficiency of the furnace for a given process heating duty. Alternatively, if the combustion air is preheated (e.g. by heat recovery), then again the theoretical flame temperature increases, reducing the stack loss. 

For our simulations with heat sinks in spheres, we chose not to stack runs, in order to minimize the change in temperature across the WS, and instead carried out a study of the effects of simplified boundary conditions. For most runs, simple boundary conditions were used in which the fluid entering at the base of the segment was set uniformly to Tin, and fluxes through the solid areas on the top and bottom planes were set to zero. No thermal boundary condition was required for the flow outlet boundary. 

The height of a flare is fixed on the basis of the heat generated and the resulting potential damage to equipment and humans. The usual design criterion is that the heat intensity at the base of the stack is not to exceed 1500 Btu/hr/ft2. The effects of thermal radiation are shown in the following table ... 

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