High-Speed Magnetic Filtration System Using HTS Bulk Magnet for Used Wash Water of Drum

2009 ◽  
Vol 19 (3) ◽  
pp. 2165-2168 ◽  
Author(s):  
F. Mishima ◽  
T. Terada ◽  
T. Ohnishi ◽  
K. Iino ◽  
H. Ueda ◽  
...  
Author(s):  
Liang Yuan ◽  
Jinchuan Bai ◽  
Bo Feng ◽  
Li Wan ◽  
Songping Chen ◽  
...  

2012 ◽  
Vol 26 (4) ◽  
pp. 1301-1306 ◽  
Author(s):  
T. Oka ◽  
D. Ishiduka ◽  
J. Ogawa ◽  
S. Fukui ◽  
T. Sato ◽  
...  

2012 ◽  
Vol 400 (2) ◽  
pp. 022089 ◽  
Author(s):  
T Oka ◽  
H Seki ◽  
D Ishiduka ◽  
J Ogawa ◽  
S Fukui ◽  
...  

2008 ◽  
Vol 18 (2) ◽  
pp. 828-831
Author(s):  
S. Fukui ◽  
Y. Shoji ◽  
R. Abe ◽  
J. Ogawa ◽  
M. Yamaguchi ◽  
...  

2014 ◽  
Vol 69 (12) ◽  
pp. 2548-2553 ◽  
Author(s):  
Y. Lee ◽  
S. W. Oa

A cylindrical two chambered microbial fuel cell (MFC) integrated with an anaerobic membrane filter was designed and constructed to evaluate bioelectricity generation and removal efficiency of organic substrate (glucose or domestic wastewater) depending on organic loading rates (OLRs). The MFC was continuously operated with OLRs 3.75, 5.0, 6.25, and 9.38 kg chemical oxygen demand (COD)/(m3·d) using glucose as a substrate, and the cathode chamber was maintained at 5–7 mg/L of dissolved oxygen. The optimal OLR was found to be 6.25 kgCOD/(m3·d) (hydraulic retention time (HRT) 1.9 h), and the corresponding voltage and power density averaged during the operation were 0.15 V and 13.6 mW/m3. With OLR 6.25 kgCOD/(m3·d) using domestic wastewater as a substrate, the voltage and power reached to 0.13 V and 91 mW/m3 in the air cathode system. Even though a relatively short HRT of 1.9 h was applied, stable effluent could be obtained by the membrane filtration system and the following air purging. In addition, the short HRT would provide economic benefit in terms of reduction of construction and operating costs compared with a conventional aerobic treatment process.


2015 ◽  
Vol 78 (12) ◽  
pp. 2108-2116 ◽  
Author(s):  
MYKOLA V. SHYNKARYK ◽  
TARAS PYATKOVSKYY ◽  
HUSSEIN M. MOHAMED ◽  
AHMED E. YOUSEF ◽  
SUDHIR K. SASTRY

Produce safety has received much recent attention, with the emphasis being largely on discovery of how microbes invade produce. However, the sanitization operation deserves more attention than it has received. The ability of a sanitizer to reach the site of pathogens is a fundamental prerequisite for efficacy. This work addresses the transport processes of ozone (gaseous and liquid) sanitizer for decontamination of leafy greens. The liquid sanitizer was ineffective against Escherichia coli K-12 in situations where air bubbles may be trapped within cavities. A model was developed for diffusion of sanitizer into the interior of produce. The reaction rate of ozone with the surface of a lettuce leaf was determined experimentally and was used in a numerical simulation to evaluate ozone concentrations within the produce and to determine the time required to reach different locations. For aqueous ozone, the penetration depth was limited to several millimeters by ozone self-decomposition due to the significant time required for diffusion. In contrast, gaseous sanitizer was able to reach a depth of 100 mm in several minutes without depletion in the absence of reaction with surfaces. However, when the ozone gas reacted with the produce surface, gas concentration was significantly affected. Simulation data were validated experimentally by measuring ozone concentrations at the bottom of a cylinder made of lettuce leaf. The microbiological test confirmed the relationship between ozone transport, its self-decomposition, reaction with surrounding materials, and the degree of inactivation of E. coli K-12. Our study shows that decontamination of fresh produce, through direct contact with the sanitizer, is more feasible with gaseous than with aqueous sanitizers. Therefore, sanitization during a high-speed washing process is effective only for decontaminating the wash water.


Author(s):  
C Arcoumanis ◽  
L N Barbaris ◽  
R I Crane ◽  
P Wisby

A cyclone-based filtration system has been developed and its potential for reduction of exhaust particulates in high-speed direct injection diesel engines is evaluated; the filtration efficiency of the four cyclones has been enhanced by means of particulate agglomeration induced by cooling in a heat exchanger. With this system installed in the exhaust pipe of a 2.5 litre direct injection engine, tests covering a wide range of speed, load and exhaust gas recirculation (EGR) fraction resulted in reductions of up to 77 per cent in emitted particulate mass flowrate. The dependence of the system's performance on engine operating conditions, EGR configuration and cyclone geometry is presented and discussed.


2009 ◽  
Vol 469 (15-20) ◽  
pp. 1849-1852 ◽  
Author(s):  
T. Oka ◽  
H. Kanayama ◽  
K. Tanaka ◽  
S. Fukui ◽  
J. Ogawa ◽  
...  

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