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Online since: December 2012
Authors: Chun Juan Dong, Qing Ye Pan
Linearization of Eq. (2) gives the relationship: (4) Where: the substrate removal rate (g.l−1.d−1); : the maximum utilization rate constant (g.l−1.d−1);: the saturation value constant (g.l−1.d−1); and is the sludge-bed volume of the EGSB reactor.
For low influent flow of 9L.h-1, 11L.h-1, the optimal was 4.0m.h-1 and 3.6m.h-1, and the corresponding topmost COD removal was 90% and 89%.
But with lower of 3.6m.h-1, 3.0m.h-1 and 3.1m.h-1, 2.8m.h-1, the COD removal only decreased to 89%, 86% and 88%, 85%, respectively.
At 26˚C, for 9L.h-1, 12 L.h-1, 15L.h-1, 24L.h-1 influent flow, the EGSB reactor could all have high COD removal efficiencies of 86.0%, 85.6%, 83.9%, 84.7%.
Bioeng. 44(1994), 469-479 [2] Rebac, S., van Lier, J.B., Janssen, M.G.J., Dekkers, F., Swinkels, K.T.M., Lettinga, G.
Online since: March 2013
Authors: Suppalak Angkaew, Boonnak Sukhummek, Wunpen Chonkaew, Kritsana Pongcharoen, Kannika Lumpuengkul
Figure 1.
After that the reading data were collected every 5 minutes for 1 hour and 40 minutes.
Table 1.
References [1] B.
Cochran, Ceramic hollow spheres and their applications, Current Opinion in Solid State and Materials Science. 3 (1998) 474-479
Online since: April 2012
Authors: Hasan A. Alwi, Roslan Abd-Shukor, Lay S. Ewe, Zahari Ibrahim, Noor B. Ibrahim
Table 1.
Sr (x) Grain size (µm) TIM (K) ρ (g cm-3) σ (S cm-1) α (mm2 s-1) ±20% κ (WmK-1) κe (W mK-1) 0 33 247 5.74 11 0.901 2.6 0.0083 0.02 34 264 5.72 12 1.14 3.3 0.0086 0.04 43 290 6.05 19 1.18 3.6 0.014 0.06 46 284 6.09 11 1.15 3.5 0.0079 0.08 40 291 5.68 18 1.21 3.5 0.013 0.10 31 289 5.53 54 1.34 3.7 0.040 Table 2.
References [1] C.
Alloy Compd. 479 (1-2) (2009) 357-362
Mater. 272-276(Suppl. 1) (2004) e473-e474
Online since: February 2013
Authors: Reza Shoja Razavi, Hossein Edris, Mohammad Reza Loghman-Estark
To complete drying, xerogel was placed at 250°C for 1 h.
The distinguishing characteristic peaks for cubic occur at 2θ = 30.2°, 35.2°, 50.3° and 60.02° for the (1 1 1), (2 0 0), (2 2 0) and (3 1 1) reflections [1, 3].
Fig. 1.
References [1] M.
Alloys Compds. 503 (2010) 474–479.
Online since: October 2013
Authors: Jiang Feng Song, Shu Qiu Wang, Fan Hao Zeng, Xiao Fen Tan, Lin Wei Li
The getter alloys were prepared by arc melting in an arc melting furnace with a proportion of ingredients of n(Zr):n(Ti):n(Mn):n(Fe) = (1-x):x:1:1, (x=0.1, 0.2, 0.3, 0.4).
Therefore the elements ratio of n(Ti, Zr):n(Mn):(Fe)=1:1:1 tend to obtain the quaternary laves compound of high purity.
Fig.1 SEM images (a) (b) and EDS analysis (c) (d) of the (Ti0.4Zr0.6)MnFe alloys Fig.1 shows a typical morphology and EDS spectrum of the (Ti0.4Zr0.6)MnFe alloys.
References [1] C.
Vol. 475-479 (2010), p.34 [22] Y.
Online since: April 2021
Authors: Maxim A. Ryzhkov, Dmitriy I. Lebedev, Mikhail V. Maisuradze
These steels contained the reduced amount of nickel (1 wt. % and lesser) and small additions of vanadium and niobium.
The temperature dependences of the austenite transformation fraction determined using equation (1) for the cooling rates 0.1…30 °C/s are presented in Fig. 1.
Fig. 1.
References [1] J.
Heat Treat. 59 (2017) 479–485
Online since: April 2011
Authors: Niculae Ene, Mircea Olteanu, Iulia Mirela Britchi, Petru Nita
Table 1.
Al/Ti = 1/5.
Zone HVP=100 gf; [Kgf/mm2] Sample Titanized at 1100°C, 5h, 77% in weight Ti Alumino-titanized at 1100°C, 5h, Al/Ti = 1/5 Outer layer 850 891 Inner layer 473 507 Substrate 158 155 Conclusions 1.
References [1] N.
Forum Vols. 475-479 (2005), p. 2295
Online since: October 2013
Authors: Zoltán Pálmay
In such case Eq. 1 is rendered unusable in its original form, and thus needs to be adapted for cutting at changing speeds.
The cutting speed was 300 and 540 m/min, feed 0.11 mm/rev and the depth of cut 1 mm.
The error resulting from applying the approximate method at speed change of, for example, vc=100÷140 m/min stays below 1%.
References [1] ISO Standard 3685, Tool-Life Testing with Single-Point Turning Tools
Technol. (2002) 20 pp.475-479
Online since: September 2013
Authors: Chao Gang Zhou, Jing Li, He Wu, Ke Zhi Yang, Xiao Guang Hu, Ke Sen Cai, Guo Ping Wu
Research and Application of Rephosphoration Dynamics Model Chaogang Zhou 1,2, Jing Li 1,2, He Wu 1,2, Kezhi Yang 1,2, xiao-guang Hu 1,2,a, Ke-sen Cai 3, Guoping Wu 3 1State Key Laboratory of Advanced Metallurgy, University of Science and Technology Beijing ,Beijing 10083,China; 2 School of Metallurgy and Ecologic Engineering, University of Science and Technology Beijing, Beijing 10083,China; 3 Nanjing Iron and Steel Co.
In order to improve the efficiency of dephosphorization, the metallurgical workers around the hot metal and molten steel dephosphorization has carried on the dynamics, and also reached a consensus [1-3].
Theoretical basis and basic assumptions of the model According to the theory of ion,the response equation of rephosphoration can be represented as follows: (1) The application of the theory of double membrane[4], the mass transfer process of liquid steel to phosphorus are shown in fig 1 below.
References [1] W.
ISIJ International, 1993, 33(4): 479-487
Online since: May 2016
Authors: Erik Janzén, Igor A. Abrikosov, David D. Awschalom, Ádám Gali, Krisztian Szasz, Viktor Ivády, Abram L. Falk, Paul V. Klimov, David J. Christle, William F. Koehl
We observe 99%±1% degree of polarization.
Figure 1.
We found polarizable 29Si nuclear spins around the defect [see Fig. 1(a)].
References [1] P.G.
Nature 479 (2011) 84
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