An Organic Liquid Membrane System for the Separation and Production of Histamine

1991 ◽  
Vol 26 (9) ◽  
pp. 1195-1205 ◽  
Author(s):  
Shigeo Takeshima ◽  
Shingo Hirose
1994 ◽  
Vol 29 (16) ◽  
pp. 2117-2129 ◽  
Author(s):  
Shigeo Takeshima ◽  
Shinichiro Wada ◽  
Hiromu Sakurai

2012 ◽  
Vol 673 ◽  
pp. 8-12 ◽  
Author(s):  
Noriyoshi Ueya ◽  
Osamu Shirai ◽  
Yuki Kushida ◽  
Seiya Tsujimura ◽  
Kenji Kano

1987 ◽  
Vol 17 (2) ◽  
pp. 193-203 ◽  
Author(s):  
Kazuo Nomura ◽  
Shao-Mu Ma ◽  
Hiroshi Kamaya ◽  
Issaku Ueda ◽  
Sheng H. Lin

2018 ◽  
Vol 80 (3) ◽  
Author(s):  
Adhi Kusumastuti ◽  
A. L. Ahmad ◽  
Rodia Syamwil ◽  
Samsudin Anis

Although textile dyes is basically available in very low concentration (10-200 ppm); it should be removed due to the toxicity to human body and environment. Among the existing methods, emulsion liquid membrane (ELM) is a promising method by providing high interfacial area and the ability to remove a very low concentration of the solute. The optimal emulsions were produced using commercially supplied homogeniser. Initially, methylene blue in simulated wastewater was extracted using a Taylor-Couette column. Methylene blue concentration was determined using spectrophotometer. Complete extraction was performed in the designed column. The research obtained optimal extraction efficiency of about 99% at external phase pH of 10, carrier concentration of 9 wt. %, HCl concentration of 0.5 M, initial feed concentration of 20 ppm, volume ratio of emulsion to feed phase of 1:5, extraction time of 5 min, and extraction speed of 600 rpm. 


Nature ◽  
1977 ◽  
Vol 270 (5634) ◽  
pp. 277-278 ◽  
Author(s):  
TOSHIO SHINBO ◽  
KENZO KURIHARA ◽  
YONOSUKE KOBATAKE ◽  
NAOKI KAMO

2010 ◽  
Vol 46 (1) ◽  
pp. 67-73 ◽  
Author(s):  
S. Makaka ◽  
M. Aziz ◽  
A. Nesbitt

The extraction of copper ions in a tubular supported liquid membrane using LIX 984NC as a mobile carrier was studied, evaluating the effect of the feed characteristics (flowrate, density, viscosity) on the feedside laminar layer of the membrane. A vertical countercurrent, double pipe perspex benchscale reactor consisting of a single hydrophobic PVDF tubular membrane mounted inside was used in all test work. The membrane was impregnated with LIX 984NC and became the support for this organic transport medium. Dilute Copper solution passed through the centre pipe and sulphuric acid as strippant passed through the shell side. Copper was successfully transported from the feedside to the stripside and from the data obtained, a relationship between Schmidt, Reynolds and Sherwood number was achieved of.


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