contributor author | J. F. Thorpe | |
contributor author | J. E. Funk | |
contributor author | T. Y. Bong | |
date accessioned | 2017-05-09T00:40:13Z | |
date available | 2017-05-09T00:40:13Z | |
date copyright | March, 1970 | |
date issued | 1970 | |
identifier issn | 0098-2202 | |
identifier other | JFEGA4-27360#173_1.pdf | |
identifier uri | http://yetl.yabesh.ir/yetl/handle/yetl/144523 | |
description abstract | An experimental investigation was conducted to determine the void fraction and pressure drop occurring in a forced-convection water electrolysis cell. It was concluded that the slip ratio is essentially unity for water electrolysis cells operating at atmospheric pressure and 80–100 deg F. A frictional pressure-drop multiplier was determined by a data reduction technique that has been used extensively in the boiling heat transfer literature. This multiplier has been correlated and found to be a function of both the void fraction and the gas generation rate. | |
publisher | The American Society of Mechanical Engineers (ASME) | |
title | Void Fraction and Pressure Drop in a Water Electrolysis Cell | |
type | Journal Paper | |
journal volume | 92 | |
journal issue | 1 | |
journal title | Journal of Fluids Engineering | |
identifier doi | 10.1115/1.3424926 | |
journal fristpage | 173 | |
journal lastpage | 182 | |
identifier eissn | 1528-901X | |
keywords | Electrolysis | |
keywords | Porosity | |
keywords | Pressure drop | |
keywords | Water | |
keywords | Heat transfer | |
keywords | Atmospheric pressure | |
keywords | Boiling AND Forced convection | |
tree | Journal of Fluids Engineering:;1970:;volume( 092 ):;issue: 001 | |
contenttype | Fulltext | |