کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
4989204 | 1455975 | 2017 | 12 صفحه PDF | دانلود رایگان |
- Non-equilibrium thermodynamics description of membrane distillation.
- Distillation of water against a pressure difference.
- Water flux directly driven by a thermal driving force.
- Description of transfer at liquid-membrane interface and hydrophobic membrane.
- Reasonable comparable with experimental results from MemPower® concept.
Membrane distillation is an attractive technology for production of fresh water from seawater. The MemPower® concept, studied in this work, uses available heat (86 °C) to produce pressurized water (2.2 bar and 46 °C) by membrane distillation, which again can be used to power a turbine for co-production of electricity. We develop a non-equilibrium thermodynamic model to accurately describe the transfer at the liquid-membrane interfaces, as well as through the hydrophobic membrane. The model can explain the observed mass flux, and shows that 85% of the energy is dissipated at the membrane-permeate interface. It appears that the system's performance will benefit from a lower interface resistance to heat transfer, in particular at the permeate side of the membrane. The nature of the membrane polymer and the pore diameter may play a role in this context.
Journal: Journal of Membrane Science - Volume 524, 15 February 2017, Pages 151-162