Power-aware Test Generation for Reducing Yield Loss Risk in At-Speed Scan Testing

2019 ◽  
Vol 18 (1) ◽  
pp. 231-236
Author(s):  
Yuta Yamato ◽  
Xiaoqing Wen ◽  
Kohei Miyase ◽  
Hiroshi Furukawa ◽  
Seiji Kajihara
Author(s):  
X. Wen ◽  
K. Enokimoto ◽  
K. Miyase ◽  
Y. Yamato ◽  
M. A. Kochte ◽  
...  
Keyword(s):  

Author(s):  
X. Wen ◽  
K. Miyase ◽  
S. Kajihara ◽  
H. Furukawa ◽  
Y. Yamato ◽  
...  
Keyword(s):  

Author(s):  
Xiaoqing Wen ◽  
Y. Yamashita ◽  
S. Kajihara ◽  
Laung-Terng Wang ◽  
K.K. Saluja ◽  
...  

2019 ◽  
Vol 27 (1) ◽  
pp. 197-202
Author(s):  
Xiaoqing Wen ◽  
K. Enokimoto ◽  
K. Miyase ◽  
S. Kajihara ◽  
M. Aso ◽  
...  

Author(s):  
Nor Azura Zakaria ◽  
Edward V. Bautista Jr. ◽  
Suhaimi Bahisham Jusoh ◽  
Weng Fook Lee ◽  
Xiaoqing Wen

2008 ◽  
Vol 24 (4) ◽  
pp. 379-391 ◽  
Author(s):  
Xiaoqing Wen ◽  
Kohei Miyase ◽  
Tatsuya Suzuki ◽  
Seiji Kajihara ◽  
Laung-Terng Wang ◽  
...  

TAPPI Journal ◽  
2013 ◽  
Vol 12 (10) ◽  
pp. 33-41 ◽  
Author(s):  
BRIAN N. BROGDON

This investigation evaluates how higher reaction temperatures or oxidant reinforcement of caustic extraction affects chlorine dioxide consumption during elemental chlorine-free bleaching of North American hardwood pulps. Bleaching data from the published literature were used to develop statistical response surface models for chlorine dioxide delignification and brightening sequences for a variety of hardwood pulps. The effects of higher (EO) temperature and of peroxide reinforcement were estimated from observations reported in the literature. The addition of peroxide to an (EO) stage roughly displaces 0.6 to 1.2 kg chlorine dioxide per kilogram peroxide used in elemental chlorine-free (ECF) bleach sequences. Increasing the (EO) temperature by Δ20°C (e.g., 70°C to 90°C) lowers the overall chlorine dioxide demand by 0.4 to 1.5 kg. Unlike what is observed for ECF softwood bleaching, the presented findings suggest that hot oxidant-reinforced extraction stages result in somewhat higher bleaching costs when compared to milder alkaline extraction stages for hardwoods. The substitution of an (EOP) in place of (EO) resulted in small changes to the overall bleaching cost. The models employed in this study did not take into account pulp bleaching shrinkage (yield loss), to simplify the calculations.


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