Showing 4 results for Shell and Tube Heat Exchanger
Masoud Niknam, Hossein Ahmadi Danesh Ashtiani, , ,
Volume 12, Issue 1 (4-2012)
Abstract
In the initial steps of grass-root projects, heat exchangers cost estimation for proper decision making regarding network optimization design through pinch technology is very important. It is necessary to forecast the cost of a heat exchanger through cost estimation equations. In this article, the cost estimation equations of heat exchanger and the heat exchangers network for shell and tube heat exchangers and plate and frame heat exchangers are obtained. These equations are the function of heat transfer area by available prices in Iran. The proposed relations for Shell and tube heat exchangers are in the maximum operating pressure region of shell and tube side between 1.2–41 bars and made of two types of material: carbon steel and stainless steel 316. Furthermore, plate and frame heat exchangers relations in two regions of the inlet cold flow lower than 30 cubic meters and between 30 to 50 cubic meters are obtained. These plate and frame heat exchangers are made of stainless steel 316. Moreover, here the error of the proposed equations is studied.
Asma Dehghan, Ali Keshavarz Valian, Alireza Batooei, Hojjat Saberinejad,
Volume 17, Issue 10 (1-2018)
Abstract
Oscillating flow is one of the most important characteristics of flow in stirling engine heat exchangers. In this study reciprocating flow in stirling engine cooler is investigated numerically. Numerical solution is based on finite volume and pressure based algorithm by using the commercial CFD code fluent. A Shell and tube type heat exchanger used as cooler. The working fluid, gas flows inside the tubes while the cooling fluid, water flows around the tubes. The heat transfer coefficient, temperature difference between tube walls and working fluid, Nusselt number and friction coefficient are calculated for Helium, Carbon dioxide and Nitrogen at different operating pressure and oscillating frequency. The Nusselt number, heat transfer coefficient and temperature difference between tube walls and working fluid increase with increase of operating pressure or oscillating frequency while Friction coefficient decreases. Helium has the highest heat transfer coefficient and friction coefficient and the lowest temperature difference between tube walls and working fluid. At the highest operating pressure and oscillating frequency, Carbon dioxide has the highest Nusselt number and the lowest Friction coefficient. Finally empirical equations for Nusselt number and friction coefficient are proposed for Helium, Carbon dioxide and Nitrogen, the error of the equations are within 0.23-8.07% when the range of kinetic Reynolds number is 2.96-212.50.
A. Heidary, M.a. Ehteram,
Volume 20, Issue 2 (1-2020)
Abstract
In the present paper, the performance of a shell and tube heat exchanger in which its cold working fluid is water and its hot working fluid is flue gases from natural gas-fueled internal combustion engine with working power of 15.4 kW was investigated. At first, with changing temperature and flow rate of inlet water, the performance of heat exchanger in both condensation and non-condensation situations was experimentally studied in the laboratory in order to have a criterion for validation of the simulations results in future. By comparing different simulation models in Aspen B-JAC software, the least error simulation model was chosen to do the other costly and impossible analyzes numerically in the laboratory environment. The study of the effect of the tube’s inner diameter on the heat exchanger’s performance in condensation situation showed 5.4% increase in the heat transfer while inner diameter decreases from 7 to 6 mm. The separation of the different heat transfer stages showed 26.4% of the latent heat transfer in the maximum discharge experiments for the inner diameter of 6 mm. Finally, the engine/heat exchanger set was assessed as micro combined heat and power and assumed that the heat exchanger is used for providing hot water for a 4-person family house in Tehran and the combustion engine is used for generating electrical power. This set was able to provide hot water during 9 warm months of a year by 1-hour work per day with 29% decrease of fuel consumption in comparison with traditional burners and at the same time, this set provides almost twice the electrical power requirements.
F. Aminifar, A. Ghafouri, A. Falavand Jozaei,
Volume 20, Issue 10 (10-2020)
Abstract
Heat exchangers facilitate the transfer of heat between fluids with different temperatures. Compared with solids, most fluids have lower heat transfer coefficients and as a result, the use of high heat transfer coefficient solid particles as additives can increase the convective heat transfer coefficient of the fluid. In this study, the effect of the addition of nanoparticles to the base fluid (deionized water), application of triangular-cut twisted tapes as well as corrugation of shell and tube type heat exchangers pipes, is investigated on heat transfer values, friction coefficient variations as well as variations in performance evaluation criterion. The effects of addition of 0.7 and 1% magnesium-oxide nanoparticles on heat transfer coefficient improvements is investigated and the results of simultaneous application of magnesium-oxide water nanoparticles, corrugated pipes, and twisted tapes are compared. Comparisons against the basic conditions (deionized water without nanofluid, corrugated pipes or triangular-cut twisted tapes) indicate a 48% increase in thermal performance, a minuscule increase of 6.3% in friction coefficient and a 46% increase in the performance evaluation criterion as a result of the application of %0.7 magnesium-oxide water nanoparticles, use of corrugated pipes and triangular cut twisted tapes on the inner surface of shell and tube heat exchanger piping. Also, the application of 1% magnesium-oxide water nanofluid, and simultaneous use of corrugated pipes and triangular-cut twisted tapes on shell and tube heat exchanger piping inner surface results in a 72% increase in thermal performance, a minuscule increase of 6.9% in friction coefficient and a 70% increase in the performance evaluation criterion.
