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翻訳と辞書　辞書検索 [ 開発暫定版 ] スポンサード リンク NTU method ： ウィキペディア英語版 NTU method The Number of Transfer Units (NTU) Method is used to calculate the rate of heat transfer in heat exchangers (especially counter current exchangers) when there is insufficient information to calculate the Log-Mean Temperature Difference (LMTD). In heat exchanger analysis, if the fluid inlet and outlet temperatures are specified or can be determined by simple energy balance, the LMTD method can be used; but when these temperatures are not available The NTU or The Effectiveness method is used. To define the effectiveness of a heat exchanger we need to find the maximum possible heat transfer that can be hypothetically achieved in a counter-flow heat exchanger of infinite length. Therefore ''one'' fluid will experience the maximum possible temperature difference, which is the difference of $\backslash \; T\_-\; \backslash \; T\_$ (The temperature difference between the inlet temperature of the hot stream and the inlet temperature of the cold stream). The method proceeds by calculating the heat capacity rates (i.e. mass flow rate multiplied by specific heat) $\backslash \; C\_h$ and $\backslash \; C\_c$ for the hot and cold fluids respectively, and denoting the smaller one as $\backslash \; C\_$. A quantity: :$q\_\backslash \; =\; C\_\; (T\_-T\_)$ is then found,where $\backslash \; q\_$ is the maximum heat that could be transferred between the fluids per unit time. $\backslash \; C\_$ must be used as it is the fluid with the lowest heat capacity rate that would, in this hypothetical infinite length exchanger, actually undergo the maximum possible temperature change. The other fluid would change temperature more slowly along the heat exchanger length. The method, at this point, is concerned only with the fluid undergoing the maximum temperature change. The ''effectiveness(E)'', is the ratio between the actual heat transfer rate and the maximum possible heat transfer rate: :$E\; \backslash \; =\; \backslash frac\; -T\_)\backslash \; =\; C\_c\; (T\_\; -\; T\_)$ Effectiveness is dimensionless quantity between 0 and 1. If we know E for a particular heat exchanger, and we know the inlet conditions of the two flow streams we can calculate the amount of heat being transferred between the fluids by: :$q\; \backslash \; =\; E\; C\_\; (T\_\; -T\_)$ For any heat exchanger it can be shown that: :$\backslash \; E\; =\; f\; (\; NTU,\backslash frac\})$ For a given geometry, $\backslash \; E$ can be calculated using correlations in terms of the "heat capacity ratio" :$C\_r\; \backslash \; =\; \backslash frac\}$ and the ''number of transfer units'', $\backslash \; NTU$ :$NTU\; \backslash \; =\; \backslash frac)\; )\})\; )\})\; )\}$ For $C\_r\; \backslash \; =\; 1$ :$E\backslash \; =\; \backslash frac$ Similar effectiveness relationships can be derived for concentric tube heat exchangers and shell and tube heat exchangers. These relationships are differentiated from one another depending on the type of the flow (counter-current, concurrent, or cross flow), the number of passes (in shell and tube exchangers) and whether a flow stream is mixed or unmixed. Note that the $C\_r\; \backslash \; =\; 0$ is a special case in which phase change condensation or evaporation is occurring in the heat exchanger. Hence in this special case the heat exchanger behavior is independent of the flow arrangement. Therefore the effectiveness is given by: :$E\; \backslash \; =\; 1\; -\; \backslash exp()$ == References == * F. P. Incropera & D. P. DeWitt 1990 ''Fundamentals of Heat and Mass Transfer'', 3rd edition, pp. 658–660. Wiley, New York * F. P. Incropera, D. P. DeWitt, T. L. Bergman & A. S. Lavine 2006 ''Fundamentals of Heat and Mass Transfer '',6th edition, pp 686–688. John Wiley & Sons US 抄文引用元・出典: フリー百科事典『 ウィキペディア（Wikipedia）』 ■ウィキペディアで「NTU method」の詳細全文を読む スポンサード リンク 翻訳と辞書 : 翻訳のためのインターネットリソース Copyright(C) kotoba.ne.jp 1997-2016. All Rights Reserved.