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A two-stage membrane process is designed for CO2 capture from coal-fired power plants.
Secondly, a semi-dynamic membrane process is proposed: a stirred batch reactor is coupled with a microfiltration immersed-membrane.
The minimum energy consumption of a multi-stage membrane process is primarily determined by the membrane selectivity and recycle ratio.
PRO and FO coupling with an RO membrane process is proposed to reduce the cost of seawater desalination and the potential for power generation.
Practical application of models developed by the research community to predict the performance in low-pressure membrane process is very limited.
Our study demonstrates that strengthening the protein trafficking in ER-to-Golgi ER-to-Golgi ER-to-Golgibrand process is a novel secretory engineering strategy for improving heterologous protein production in S. cerevisiae.
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The SDI value of the membrane process was consistently lower than that of the conventional process.
After then, a pilot scale membrane process was designed using a simulation program.
Therefore, membrane process was used for solid liquid separation and effluent solid concentration was approximately zero.
In order to improve treatment quality, a cross-flow membrane process was integrated to the sono-electrocoagulation process.
The feasibility of dewatering coal tailings slurry by forward osmosis (FO) membrane process was investigated in this research.
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