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{"target":"https://pubannotation.org/docs/sourcedb/PMC/sourceid/4534144","sourcedb":"PMC","sourceid":"4534144","source_url":"https://www.ncbi.nlm.nih.gov/pmc/4534144","text":"Wall boundary condition was considered on the studied incinerator, because the solid surface is in direct contact with the fluid [24]. Given that the size and profile of the inlet pressure to the studied incinerator are known, the pressure inflow and pressure outflow were selected for inlet and outlet boundary conditions, respectively. The walls were made of steel with a thermal conductivity of 202 W/M.K. For the flows with a velocity less than the speed of sound, a turbulence of less than 5 % can be considered as assumed in the present model. Other inputs are described in Table 2.\nTable 2 The inputs to the Fluent model\nValue Parameter\n3 % Turbulent Intensity\nStationary Wall Motion\nNo slip Shear Condition\n0.00004 (m) Roughness Height\n2.76 (m) Hydraulic Diameter\n0.5 Roughness Constant","divisions":[{"label":"label","span":{"begin":589,"end":596}},{"label":"caption","span":{"begin":597,"end":627}},{"label":"p","span":{"begin":597,"end":627}},{"label":"tr","span":{"begin":628,"end":643}},{"label":"th","span":{"begin":628,"end":633}},{"label":"th","span":{"begin":634,"end":643}},{"label":"tr","span":{"begin":644,"end":667}},{"label":"td","span":{"begin":644,"end":647}},{"label":"td","span":{"begin":648,"end":667}},{"label":"tr","span":{"begin":668,"end":690}},{"label":"td","span":{"begin":668,"end":678}},{"label":"td","span":{"begin":679,"end":690}},{"label":"tr","span":{"begin":691,"end":714}},{"label":"td","span":{"begin":691,"end":698}},{"label":"td","span":{"begin":699,"end":714}},{"label":"tr","span":{"begin":715,"end":743}},{"label":"td","span":{"begin":715,"end":726}},{"label":"td","span":{"begin":727,"end":743}},{"label":"tr","span":{"begin":744,"end":771}},{"label":"td","span":{"begin":744,"end":752}},{"label":"td","span":{"begin":753,"end":771}},{"label":"td","span":{"begin":772,"end":775}}],"tracks":[]}