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Linear oligosiloxanes functionalized with bulky side chain tris(trimethylsilyl)hexyl (TTSH) substituents were transformed into cross-linked materials by UV 193 nm excimer pulsed laser ablation. The process occurred without any catalyst, by reactions of radicals formed in UV laser induced photolysis of side tris(trimethylsilyl)hexyl groups. Chemical changes were monitored by FTIR, LC/UV, GC/MS and solubility tests. 相似文献
34.
CH_4、CO_2与O_2制合成气的研究 Ⅱ工艺条件的影响 总被引:1,自引:0,他引:1
在固定床反应器中考察了12%Ni-5%RE-2%Cu-2%Li/Al2O3(mass)催化剂在CH4、CO2与O2催化氧化重整制合成气反应中催化剂粒径、工艺操作条件(空速与温度)及原料气配比对反应的影响,确定了较佳的操作条件:催化剂粒径20~40目,反应最佳温度为800℃,SV=4×104ml/(g·h)。同时看到在不同的原料气配比的条件下该催化剂的活性亦很稳定,不仅达到了反应平衡,且产物V(CO)/V(H2)比有很强的调变性。 相似文献
35.
Studies of the complete oxidation of methane on a Pt electrode-catalyst in the cell with a solid proton-conducting electrolyte (CH4 + O2, Pt ¦ SrCe0.92Dy0.08O3 ¦ Pt, H2O + N2) were carried out. The non-Faradaic effect of electrochemical hydrogen pumping on the rate of methane oxidation has been demonstrated. The induced change in the reaction rate at anodic polarization of a Pt electrode-catalyst was over two orders of magnitude higher than the rate of hydrogen pumping from the reaction zone through the electrolyte. 相似文献
36.
甲烷和乙烷可以同时在W-Mn/SiO2催化剂上得到活化生成乙烯。原料乙烷和甲烷体积比在0.11~0.25的范围内,当甲烷转化率为20%左右时,共进料反应产物中乙烯体积浓度为8%~12%,达到炼油厂催化裂化干气中乙烯的浓度。 相似文献
37.
The partial oxidation of methane over the supported Rh (0.8 wt.%) catalysts was investigated. Two kinds of supports were used, MgO and Ti-modified MgO (prepared by grafting technique). Among the Ti-modified MgO supports, two different compounds were used as source of Ti: inorganic (chloride) and organic (alkoxide). The catalytic performance of Rh-supported catalysts depends on the support and varies in the sequence: Ti-MgO/I > Ti-MgO/O > MgO. Ti-containing catalysts exhibited higher activity and selectivity compared to MgO, which is especially noticeable at low temperature. Possible explanations for the phenomena observed were proposed on the basis of characterization results. 相似文献
38.
以淮南矿区C13、B11b、B10、B4b和A3煤为研究对象,从中精选出精煤、壳质暗煤、惰性暗煤及构造煤,采用重量法,分别测定它们的甲烷吸附量,研究煤的甲烷吸附性。 相似文献
39.
A. Baylaucq C. Boned X. Canet C. K. Zéberg-Mikkelsen 《International Journal of Thermophysics》2003,24(3):621-638
The dynamic viscosity of toluene and methane mixtures containing 25.03, 37.19, 49.95, 64.11, and 95.00 mol% methane has been measured using a falling-body viscometer. The measurements (280 data points) have been performed in the temperature range 293.15 to 373.15 K and at pressures up to 140 MPa. The data have been discussed in the framework of recent representative models (hard-sphere scheme, friction theory, and free-volume model) as well as with simple mixing laws and empirical models (particularly the LBC model and the self-referencing model) used in the literature. This comparative study shows that the average absolute deviation of the models is between 4.9 and 26.8%, and the maximum deviation is between 11.6 and 49.5%. 相似文献
40.
A method of determining pore size distribution, PSD, of carbon adsorbents based on the high pressure methane isotherm is presented. A generic software package, and an IBM compatible PC, have been used to search for a PSD in the form of a histogram. The method relies on a known local isotherm, in this case, assuming a simplified model of infinite slit shaped carbon pores.Three carbons, having very different pore structures: BPL, PX-21, and PVDC, were analyzed using the new method and the results compared with those obtained from subcritical Ar, and N2 isotherms. The analysis from the high pressure methane isotherm gave results which are different than those from the low pressure low temperature isotherms but not significantly enough to be unrealistic. 相似文献