Membrane module with a feed tank for fine purification of gases

2008 ◽  
Vol 42 (4) ◽  
pp. 398-403 ◽  
Author(s):  
V. M. Vorotyntsev ◽  
P. N. Drozdov ◽  
I. V. Vorotyntsev ◽  
S. S. Balabanov
2011 ◽  
Vol 51 (8) ◽  
pp. 595-600 ◽  
Author(s):  
V. M. Vorotyntsev ◽  
P. N. Drozdov ◽  
I. V. Vorotyntsev ◽  
E. S. Belyaev

2021 ◽  
Vol 23 (1) ◽  
Author(s):  
Shinji Hayashi ◽  
Rieko Yagi ◽  
Shuhei Taniguchi ◽  
Masami Uji ◽  
Hidaka Urano ◽  
...  

AbstractCell-assisted lipotransfer (CAL) is an advanced lipoinjection method that uses autologous lipotransfer with addition of a stromal vascular fraction (SVF) containing adipose-derived stromal stem cells (ASCs). The CAL procedure of manual isolation of cells from fat requires cell processing to be performed in clean environment. To isolate cells from fat without the need for a cell processing center, such as in a procedure in an operation theater, we developed a novel method for processing SVF using a closed cell washing concentration device (CCD) with a hollow fiber membrane module. The CCD consists of a sterilized closed circuit, bags and hollow fiber, semi-automatic device and the device allows removal of >99.97% of collagenase from SVF while maintaining sterility. The number of nucleated cells, ASCs and viability in SVF processed by this method were equivalent to those in SVF processed using conventional manual isolation. Our results suggest that the CCD system is as reliable as manual isolation and may also be useful for CAL. This approach will help in the development of regenerative medicine at clinics without a cell processing center.


RSC Advances ◽  
2021 ◽  
Vol 11 (35) ◽  
pp. 21248-21258
Author(s):  
Di Zhang ◽  
Pengle Zhang ◽  
Du Xiao ◽  
Xiaogang Hao

Novel ion permselective membrane modules based on the ESIX scheme.


2019 ◽  
Vol 29 (10) ◽  
pp. 1346-1358 ◽  
Author(s):  
Sebastian Englart

This study discusses the use of a membrane module for semi-direct evaporative air cooling. A cross-flow membrane module was used to carry out this air treatment process. For such a flow, it was proposed to describe and solve the heat and mass transfer model as a one-dimensional problem. The mathematical model was used to determine the moisture content and air temperature at the outlet from the module and the temperature of the circulating water. Results obtained using the proposed model are in good agreement with the experimental data. The relative error for the air temperature at the module outlet did not exceed 0.5%. For the moisture content, the relative error did not exceed 4%. For the circulating water temperature, the relative error did not exceed 0.6%. This paper also discusses the heating efficiency of the evaporative cooling process. Methods for determining the unit cooling indicator and the energy efficiency ratio are also proposed.


Atomic Energy ◽  
1960 ◽  
Vol 6 (3) ◽  
pp. 208-210
Author(s):  
N. S. Grachev ◽  
P. L. Kirillov

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