| contributor author | Martinez | |
| contributor author | Serra, Luis | |
| contributor author | Verda, Vittorio | |
| contributor author | Picأ³n | |
| contributor author | Rubio | |
| date accessioned | 2017-05-09T01:27:57Z | |
| date available | 2017-05-09T01:27:57Z | |
| date issued | 2016 | |
| identifier issn | 0195-0738 | |
| identifier other | jert_138_06_062006.pdf | |
| identifier uri | http://yetl.yabesh.ir/yetl/handle/yetl/160958 | |
| description abstract | The direct heat exchange network (direct flow mixing network) and the indirect heat exchange network (exchanger network) are two of the elements that constitute a water network where heat and mass are transferred. When designing these systems, it is important to consider different aspects such as thermodynamics and equipment costs. This paper analyzes different design options within the framework of heuristic methodologies on a case study taken from the open literature. Two design methodologies are compared on the basis of exergy losses. It also enunciates a series of considerations in heuristic design for the heat and mass exchange networks. A very helpful tool in relation with the considerations set out herein is the composite curve; special focus will be given during its construction. This paper shows how to incorporate the exergy component in design seeking to minimize the thermal irreversibility. | |
| publisher | The American Society of Mechanical Engineers (ASME) | |
| title | Thermodynamic Analysis of Simultaneous Heat and Mass Transfer Systems | |
| type | Journal Paper | |
| journal volume | 138 | |
| journal issue | 6 | |
| journal title | Journal of Energy Resources Technology | |
| identifier doi | 10.1115/1.4034068 | |
| journal fristpage | 62006 | |
| journal lastpage | 62006 | |
| identifier eissn | 1528-8994 | |
| tree | Journal of Energy Resources Technology:;2016:;volume( 138 ):;issue: 006 | |
| contenttype | Fulltext | |