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low temperature nitrogen adsorption, adsorption of benzene vapors. The highest value of BET surface area of about 370 m 2 /g was achieved for the carbonization product obtained from co-precipitated raw components with 10 wt% compositions coal tar pitch
, USA). FTIR analyses were performed using a Unicam Matteson 4000 instrument to account for adsorbed compounds on the synthesized nanocatalysts from the reaction media and surrounding atmosphere. The specific surface area (BET) of nanocomposites was
-mouse Ly6G (1A8), anti-mouse MHCII (M5/114.15.2), anti-mouse RORγt (Q31-378), anti-mouse T-bet (4B10) and anti-mouse Ter119 (TER-119). Live/Dead discrimination was carried out using LIVE/DEAD Fixable Blue Dead Cell Stain (Thermo Fisher Scientific). Surface
high BET surface area and pore volumes. The highest BET surface area was observed for V-MCM-41 as compared with other samples. On the other hand, the lowest BET surface area was found for Ce-MCM-41 catalyst. This indicates that the formation of
/° S BET /m 2 /g −1 Pore volume/cm 3 /g D /nm Calculated surface areas/m 2 /g −1 Phase identification
area was determined by the BET method [ 20 , 21 ] and the total pore volume by the single point method. The BJH method was used to estimate the average pore size and the t -plot method was employed to assess the microporosity of the samples and
electronic microscopy (SEM) and energy dispersive analysis X-ray (EDAX) spectra (Model XL30 Philips). The results of these analyses are shown in Fig. 1 . Other surface specifics of BC were characterized by several parameters like as pH ZPC , BET surface area
and average pore size were calculated by BET method and BJH model, respectively. Results and discussion Carbonation kinetics of CaO–carbide slag Figure 2a shows the effect of carbonation
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pressure of nitrogen, hydrogen and air was kept at 3, 1.5 and 1 kg/cm 2 , in order. Catalyst characterization The BET surface area and pore volumes of the catalysts were determined from N 2 adsorption
