A single terminal fault location method for overhead transmission lines in general interconnected power system with n⁃bus was proposed. High accuracy in fault location was achieved by using both an accurate distributed parameters model for the faulted transmission line, and a two⁃bus Thevenin equivalent network model for the power system that accurately accounted for its inter connectivity. The method was tested by using transient fault data obtained from MATLAB simulations of an 11⁃bus interconnected power system. The results show that the method is capable of estimating the fault distance with high accuracy for various fault conditions. And it is sensitive to errors in the value of the local bus impedance, but insensitive to errors in the value of the remote bus impedance.

In solvent⁃free condition, a new 1D chain holmium phosphite Ho(H2PO3)4(C6N2H16)0.5 (compound 1) decorated by phosphite groups has been synthesized using N,N'⁃Dimethylpiperazine (Me2ppz) as structure directing agent, and further been characterized by powder XRD, infrared spectroscopy, thermogravimetric, inductively coupled plasma and CHN elemental analyses. Single crystal X⁃ray diffraction analysis reveals that compound 1 crystallizes in the monoclinic crystal system with the P21/c space group. The structure of compound 1 is constructed by HoO6 octahedra and [H2PO3]- pseudo⁃pyramids units via vertex oxygen atoms. It is worth noting that compound 1 is the first rare earth phosphite compound which is synthesized in solvent⁃free condition. Moreover, a pair of left⁃ and righ⁃handed helical chains are present in the structure. In addition, coordination mode and geometry of lanthanide phosphonate, phosphate and phosphite are listed in this paper.

The Mo3O/CCA was prepared by impregnation method using the (NH4)6Mo7O24·4H2O as the molybdenum source, carbon covered γ-Al2O3 (CCA) as support, and n-hexane as the carbon source. After carbonization of Mo3O/CCA obtained Mo2C/CCA. The catalysts prepared at different carbonization temperature were characterized by XRD. The effects of preparation and reaction conditions on dehydrogenation activity of the catalyst were studied in a fixed-bed down-flow reactor. The results show that the conversion of cyclohexane up to 91% was attained under the optimum condition as follows: CCA carbon covered 7.82%, final carbonization temperature 650 ℃, reaction temperature 475 ℃, reaction pressure 0.1 MPa, liquid hourly space velocity 2 h-1 and volume ratio of hydrogen to cyclohexane 200∶1.