標題: Titlebook: Design and Operation of Heat Exchangers; Proceedings of the E Wilfried Roetzel,Peter John Heggs,David Butterwort Conference proceedings 199 [打印本頁] 作者: Amalgam 時間: 2025-3-21 17:04
書目名稱Design and Operation of Heat Exchangers影響因子(影響力)
書目名稱Design and Operation of Heat Exchangers影響因子(影響力)學科排名
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書目名稱Design and Operation of Heat Exchangers網(wǎng)絡公開度學科排名
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書目名稱Design and Operation of Heat Exchangers被引頻次學科排名
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書目名稱Design and Operation of Heat Exchangers年度引用學科排名
書目名稱Design and Operation of Heat Exchangers讀者反饋
書目名稱Design and Operation of Heat Exchangers讀者反饋學科排名
作者: 過濾 時間: 2025-3-21 23:08
Conference proceedings 1992hangers was the first one on this topic and was held at the Universitat der Bundeswehr Hamburg (University of the Federal Armed Forces Hamburg) from February 27 to March 1 in 1991. The seminar was an international event and was attended by more than 60 scientists not only from countries of the Europ作者: 揮舞 時間: 2025-3-22 00:31 作者: slipped-disk 時間: 2025-3-22 06:52 作者: 都相信我的話 時間: 2025-3-22 11:13 作者: 屈尊 時間: 2025-3-22 14:29 作者: 屈尊 時間: 2025-3-22 19:46
Compact New Formulae for Mean Temperature Difference and Efficiency of Heat Exchangersoped by Gaddis and Schlünder, the new formulae may be used as efficient engineering tools in computer programs. The application of now widely available software, such as a spreadsheet calculation program for easy execution of heat exchanger design calculations with the cell method will also be demonstrated in this context.作者: 王得到 時間: 2025-3-22 23:37
Conference proceedings 1992fic events such as seminars and conferences in the thermal sciences. The series of Eurotherm Seminars established by the Committee has become a popular forum for high-level scientific and technical interchange of ideas in a wide range of specialist topics. While the presentation and publication of p作者: 預防注射 時間: 2025-3-23 01:54
Selected Problems in Heat Exchanger Designems like pressure drop to heat transfer conversion effectiveness, pressure drop utilization, problems connected with surface over-design due to exaggerated safety factors or summer/winter operations, analysis of under-designed exchangers, differential vs. integral condensation, and similar.作者: Brain-Waves 時間: 2025-3-23 08:40
Heat Exchanger Control by Stream(s) By-Pass use of by-pass for flow disturbances to both streams. For negative disturbances with respect to the design flowrates, the algorithm predicts the by-pass flows that achieve the desired outlet temperatures. By-pass will be ineffective for positive disturbances.作者: 相符 時間: 2025-3-23 10:47 作者: Iniquitous 時間: 2025-3-23 15:09
Pressure Losses in Tube Bundles of Close Spacingsocess, have transverse spacing ratios of 1.05. By a simple relation between loss coefficient, Reynolds-number and transverse spacing ratio the experimentell results can be extended to higher spacing ratios up to 1.50. The calculated results are in good correspondence with those of other authors obtained by experiments.作者: Induction 時間: 2025-3-23 19:43 作者: Sedative 時間: 2025-3-23 23:37 作者: 有惡意 時間: 2025-3-24 02:33 作者: enhance 時間: 2025-3-24 09:27 作者: ABIDE 時間: 2025-3-24 13:19 作者: Macronutrients 時間: 2025-3-24 16:24 作者: Institution 時間: 2025-3-24 19:50
Foundation iPhone App Developmenthis one establishes, given the initial conditions and the necessary heat exchange surface, the final medium difference of temperature between the two fluids, as well as the final medium temperatures of them. There have been drawn diagrams that might be used properly. There has been solved a practical problem.作者: 清晰 時間: 2025-3-25 02:03 作者: 信徒 時間: 2025-3-25 07:04
Variable Pitch Tube Layout Concept for Shell and Tube Heat Exchangerves from inner zone to outer periphery, heat transfer coefficient variation is reduced to 1.5:1 at any cross section of exchanger. The flow distribution has been studied using network analysis and is used to evaluate different configurations.作者: 滔滔不絕的人 時間: 2025-3-25 07:48 作者: 掃興 時間: 2025-3-25 14:07
Dispersion Model for Divided-Flow Heat Exchangerperature profiles are derived for the 1-1 divided-flow heat exchanger. Measurements are carried out on a segmentally baffled 1-1 divided-flow heat exchanger with various clearances between segmental baffles and shell, in order to investigate the relationship between the dispersion factor and the flow pattern.作者: 捏造 時間: 2025-3-25 17:58
https://doi.org/10.1007/978-1-349-12450-3ents are discussed. Next, a group of problems which are not easily identified in the course of the usual design process, is analyzed. These include items like pressure drop to heat transfer conversion effectiveness, pressure drop utilization, problems connected with surface over-design due to exagge作者: 真 時間: 2025-3-25 22:33 作者: 失望未來 時間: 2025-3-26 03:11 作者: 折磨 時間: 2025-3-26 06:16 作者: fluffy 時間: 2025-3-26 08:42 作者: maladorit 時間: 2025-3-26 13:37 作者: 冷淡一切 時間: 2025-3-26 19:58
Settings and Local Notificationsss flow rate on the shellside, variable entrance location of the shellside flow and piecewise variation of heat transfer coefficient (or NTU), considering shellside maldistribution such as bypassing and leakage. Especially, the explicit formulas for calculating thermal effectivenesses as well as tem作者: JAUNT 時間: 2025-3-26 22:18
Foundation iPhone App Developmentexchangers. Approximate equations for the thermal calculation of these flow arrangements with arbitrary numbers of passes are proposed. Their accuracy and limitations are discussed. The accuracy of the given equations is more than sufficient for practical design.作者: 惹人反感 時間: 2025-3-27 02:51
Foundation iPhone App Developmentw one. The analytic solution of the resulting system of differential equations is very difficult; that’s why there has been used a numerical method. This one establishes, given the initial conditions and the necessary heat exchange surface, the final medium difference of temperature between the two 作者: FLACK 時間: 2025-3-27 08:19 作者: 攝取 時間: 2025-3-27 10:58 作者: Halfhearted 時間: 2025-3-27 16:44 作者: folliculitis 時間: 2025-3-27 19:23 作者: concert 時間: 2025-3-27 23:46 作者: 箴言 時間: 2025-3-28 04:47
Settings and Local NotificationsIn many industrial applications, heat exchangers (HX) are generally a part of a system. They are therefore exposed to many transient regimes when a part of the system changes its operating conditions.作者: 細絲 時間: 2025-3-28 06:22 作者: creatine-kinase 時間: 2025-3-28 14:01 作者: Urologist 時間: 2025-3-28 17:44 作者: 相同 時間: 2025-3-28 22:29 作者: Cholesterol 時間: 2025-3-29 00:44 作者: Intellectual 時間: 2025-3-29 04:06
https://doi.org/10.1007/978-3-642-84450-8Evaporators; Heat exchanger; Kondensatoren; W?rmespeicher; W?rmeübertragung; W?rmeübertr?ger; condensors; f作者: tariff 時間: 2025-3-29 11:01 作者: Calculus 時間: 2025-3-29 12:06
EUROTHERM Seminarshttp://image.papertrans.cn/d/image/268591.jpg作者: Fretful 時間: 2025-3-29 17:17 作者: FECT 時間: 2025-3-29 20:17
Foundation iPhone App Developmentexchangers. Approximate equations for the thermal calculation of these flow arrangements with arbitrary numbers of passes are proposed. Their accuracy and limitations are discussed. The accuracy of the given equations is more than sufficient for practical design.作者: 策略 時間: 2025-3-30 01:54
Jordan Hamson-Utley,Errin Heymanshow that at low Reynolds number (~ 400) the Nusselt number in the neighborhood of the second tube of a two-tube in-line configuration is close to the Nu given by the periodically fully developed flow.作者: 漫不經(jīng)心 時間: 2025-3-30 08:05
Design Improvements of a Shell and Tube Heat Exchanger Based on Practical Experience and Numerical A Several different geometries are examined both theoretically and experimentally, utilizing some heat exchangers of Shell Chemie B.V. Wear mechanisms are located, recognized and quantified with the aid of an eddy current measuring technique. In situ measurements during operation are performed in order to verify the 2-D numerical modelling.作者: 漂泊 時間: 2025-3-30 10:22
Approximate Equations for the Design of Cross- Flow Heat Exchangersexchangers. Approximate equations for the thermal calculation of these flow arrangements with arbitrary numbers of passes are proposed. Their accuracy and limitations are discussed. The accuracy of the given equations is more than sufficient for practical design.作者: GUILE 時間: 2025-3-30 15:08
Numerical Studies of a Compact Fin-Tube Heat Exchangershow that at low Reynolds number (~ 400) the Nusselt number in the neighborhood of the second tube of a two-tube in-line configuration is close to the Nu given by the periodically fully developed flow.作者: 抒情短詩 時間: 2025-3-30 19:14 作者: 使習慣于 時間: 2025-3-30 22:28
Compact New Formulae for Mean Temperature Difference and Efficiency of Heat Exchangersen presented by the author[1, 2]. The advantages of these new formulae in the calculations required in thermal design of heat exchangers will be demonstrated for a number of flow configurations. Shell-and-tube exchangers with multiple passes, with split flow and two tube passes, as well as a number 作者: 熟練 時間: 2025-3-31 01:55 作者: RALES 時間: 2025-3-31 09:04 作者: fixed-joint 時間: 2025-3-31 13:14 作者: infatuation 時間: 2025-3-31 15:27
Simple Algorithms for Optimization of Shell and Tube Heat Exchangerspling between the geometry and the heat transfer in the near-optimal region of the feasible design space irrespective of the objective function used. Hence, the algorithm is quite general in nature and can handle various objective functions like weight, cost and volume. A decision table is provided 作者: progestin 時間: 2025-3-31 19:11
Dispersion Model for Divided-Flow Heat Exchangerss flow rate on the shellside, variable entrance location of the shellside flow and piecewise variation of heat transfer coefficient (or NTU), considering shellside maldistribution such as bypassing and leakage. Especially, the explicit formulas for calculating thermal effectivenesses as well as tem作者: 不規(guī)則的跳動 時間: 2025-4-1 00:12
Approximate Equations for the Design of Cross- Flow Heat Exchangersexchangers. Approximate equations for the thermal calculation of these flow arrangements with arbitrary numbers of passes are proposed. Their accuracy and limitations are discussed. The accuracy of the given equations is more than sufficient for practical design.
