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Subsecao III - Das Competencias do Primeiro Secretario. III - Redigir e assinar com o presidente a correspondencia oficial da Associacao. Art. 43 - Compete ao segundo secretario da Associacao: IV - Organizar os servicos da secretaria e assina-los. I - Dirigir os servicos da tesouraria. V - Apresentar no comeco de cada mes, o balancete do mes vencido, bem como a demonstracao da receita e da despesa da Associacao, afixando-os na sede social. I - Responder pela tesouraria da Associacao nos termos do artigo anterior, nos casos de impedimentos do respectivo titular. This is a business based ae aposta esportiva como jogar on trust and 5dimes cannot be trusted. Brasil e servia escanteios.
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When performing forced air cooling, it is assumed that the working atmospheric pressure and relative humidity of the power device are lower than 90%. The air around the radiator is in a stable turbulent state. Since the air flow around the radiating fins is in a turbulent state, the correlation formula of the turbulent local friction coefficient C f is: where R e is the Reynolds number, which is equal to the ratio of inertial force to viscous force. The local Nusselt number can be expressed in the following form: where α x is the air convection heat transfer at a certain position along the length of the fin; λ is the thermal conductivity of air; Y is the characteristic length; P r is the Prandtl number. Equation (6) can be rewritten in the following form: where S t x is the Stanton number, which is a criterion for describing forced convection. The larger the Stanton number, the stronger the convection heat transfer process between the fluid and the solid surface. ρ is the density of air; C p is the specific heat capacity of air. S t x P r 2 / 3 = C f 2. α x = C f ρ C p v ¯ 2 P r 2 / 3. Substituting Formula (5) and Formula (10) into Formula (9), the local heat transfer coefficient is: where x is the distance from a certain point to the fin. The measured data of the air properties of the radiator working environment temperature between −50 °C and 300 °C are obtained. After curve fitting the data, the function expressions of air density ρ , specific heat capacity C p , kinematic viscosity γ and Prandtl number P r with respect to temperature T are obtained [18] as: α x = 0.0296 x − 1 / 5 ρ ( T ) C p ( T ) v ¯ 4 / 5 γ ( T ) − 1 / 5 P r ( T ) 2 / 3. α = 0.037 S − 1 / 5 ρ ( T ) C p ( T ) v ¯ 4 / 5 γ ( T ) − 1 / 5 P r ( T ) 2 / 3.
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