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Two reactors of laboratory scale (height 1.95 m, internal diameter 0.1 m, volume 0.08 m3) and pilot-plant scale (height 7.18 m, internal diameter 0.2 m, volume 0.7 m3) were used.
We examined the associations of SH levels with left ventricular mass (LVM) and mass (M):volume (V) ratio, which are risk markers for HFpEF.
A pilot-scale reactor was constructed (height 6 m, volume 1.7 m3), and for two phases (water and air) successful validation of the model was reported.
Up to an M volume fraction of fM = 0.31, architecture H/MO/M was microphase-separated, indicating that M can be distributed into both H and O domains without overly compatibilizing the system.
Then a scale-up/scale-down approach was applied to design and construct a pilot-scale BASE reactor (height 6 m, volume 1.7 m3), to validate the hydrodynamic model.
High-yield wells in the Fanzhuang Block always have the following conditions: gas content > 20 m3/t; burial depth of 500 700 m; CRR > 0.7; LCH > 400 m; volume of frac sand > 40 m3; EDR of 30 60 m; and a decline rate of working fluid level lower than 2 m/day during the initial production stage.
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A complex liquid phase was formed by the addition of equimolar (1 M) volumes of cadmium sulphate, thiourea and cobaltous sulphate.
For trees with heights ≥ 8.1 m, volumes were estimated as a function of d1.3, h, and d6.
When the height of a tree was less than 8.1 m, volumes were estimated as a function of d1.3 and h.
An echo-planar imaging (EPI) sequence was applied for functional scans, measuring BOLD signals (echo time TE = 50 ms, repeat time TR = 90 ms, volume time 4.32 s).
An echo-planar imaging (EPI) sequence was applied for functional scans, measuring BOLD signals (echo time TE = 50 mS, repeat time TR = 90 ms, volume time 3.42 s).
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