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Fig. 1.
Table 1 encapsulates the differences between various PCM.
Table 1.
References [1] C.
Yang, Comparison of heat sink and water type PV/T collector for polycrystalline photovoltaic panel cooling, Renewable Energy. 116 (2018) 479-491. [12] K.

Fig. 1 shows the process of point merging.
For each resulting vehicle ROI from step 1), its real width dtarget_i can be calculated using (8).
If the tracking window has not matched in frame t, δt is set to 0, otherwise it is set to 1.
The analyzed data consists of more than 1 h of video taken on BeiJing highways and city expressways.
Control Engineering Practice 4.4 (1996), pp. 473-479

In this work, a vacuum melted Cu-26.5wt%Zn-4wt%Al-1.5wt%Zr alloy was studied.
Bulge forming tests were performed on equipment, with a 30 mm inner die diameter, Do, as shown in Fig. 1.
References [1] A.
Pearce, “Superplasticity-an overview” AGARD Lecture Series No. 168-Superplasticity, AGARD (1989)1-23
Sci. 10 (1970) 479-490

Raabe 1,a, F.
Eng. 1995, 3:1
[5] Hosford W F, Textures and Microstructures 1996, 26:479
Rev. 1990, 35:1
Mech. 1983, 23:1

HCl was slowly dropped into the flask with stirring to keep the pH value of the solution in the range between 1 and 2.
Fourier transform infrared (FTIR) spectra were recorded between 400 and 4000cm-1 with a resolution of 2 cm-1 on a Prostar LC240 Infrared Spectrometer (USA).
The relationship between gel time and temperature of PF and HPSi/PF resins is shown in Fig. 1.
In the process of the curing reaction, the peak intensities of –OH at 3375 cm-1 decrease gradually, while those of the absorption bands assigning to C-O-Si at 1140 cm-1 groups increase apparently, which can prove that the co-reaction between Si-OH in HPSi and phenolichydroxyl occurs successfully.
REFERENCE [1].

Fig. 1.
The calculation results are shown in Table 1.
C1-69876, competition Start-19-1 (stage 4).
SSC RAS. 15 (2013) 476-479
Pozvonoc. 13(1) (2016) 50-58.

Alumina (A) was from Sasol trade mark (USA) with particle size less than 1 mm and used as received.
Fig. 1.
The experimental data curves were fitted to the Herschel-Bulkley model and the flow index (n), in this rheological model, specify the flow type of the suspensions, as follows; flow index is less than 1, for plastic flow type; greater than 1, for shear thickening flow type and equal to 1 for Newtonian flow [14].
References [1] Liliana B.
Mechan. 12 (1979) 479-498

Fig. 1.
References [1] G.
Vol 483, 1 (2009) 14-19
Vol 679 (2017) 1-6
A Vol 319 (1970) 479-493

The results of corrosion potential, pitting potential, repassivation potential and passive current densisty from the CPP curves are given in Table 1.
(a),(c) crest and (b),(d) root Table 1.
References [1] M.
Shreir, Corrosion Handbook Vol.1, Newnes-Butterworths Boston (1979), p.3-31 [3] H.
Vol. 475-479 (2005), p. 2287 [4] C.

The problem is , (1) St
Fig 1.
The process flowsheet of the TEP is shown in Figure 1.
Table 1.
Kobi, “Fault detection and identification with a new feature selection based on mutual information,” Journal of Process Control, vol. 18, 2008, pp.479–490