In vitro evaluation and pharmacokinetics in dogs of solid dispersion pellets containing Silybum marianum extract prepared by fluid-bed coating.

The solid dispersion of a poorly water-soluble Silybum marianum extract (SME) was prepared by a one-step fluid-bed coating technique depositing onto non-pareil pellets. In vitro evaluation indicated that this technique was highly efficient and reproducible producing pellets with acceptable appearance, flowability, friability, uniformity of drug content and enhanced dissolution. Physical characterization by DSC, powder X-ray diffractometry and FT-IR suggested the formation of a solid dispersion and possible interaction between PVP and the flavonolignans.

Effect of preparation methods on the structure and catalytic performance of TiO(2)/AC photocatalysts.

Activated carbon (AC)-supported TiO(2) catalysts were prepared by sol-gel and metal organic chemical vapor deposition (MOCVD) in order to investigate effect of preparation methods on the structure and catalytic performance of TiO(2)/AC catalysts. It was found that both methods yield "egg-shell" TiO(2)/AC catalysts, that is to say, the TiO(2) coatings were mainly on the surface of AC supports. The TiO(2) coating by sol-gel was only coated on the external surface of AC.

Effect of various gases and chemical catalysts on phenol degradation pathways by pulsed electrical discharges.

The processes of phenol degradation by pulsed electrical discharges were investigated under several kinds of discharge atmospheres (oxygen, argon, nitrogen and ozone) and chemical catalysts (ferrous ion and hydrogen peroxide). The temporal variations of the concentrations of phenol and the intermediate products were monitored by HPLC and GC-MS, respectively. It has been found that the effect of various gases bubbling on phenol degradation rate ranked in the following order: oxygen-containing ozone>oxygen>argon>nitrogen.

Decolorization of cationic red X-GRL by wet air oxidation: performance optimization and degradation mechanism.

The decolorization of a strong colored azo dye solution of cationic red X-GRL was investigated by wet air oxidation under relatively mild conditions (60-180 degrees C, PO2 = 0-1.2 MPa). Mono-factor experiments were carried out to investigate the effect of the operation factors and the relatively important parameters were selected for optimization using response surface methodology to explore the interactions of these relatively important parameters.

[Construction and identification of recombinant adenovirus containing the polyproteins coding regions of O type foot-and-mouth disease virus by homologous recombination in Escherichia coli].

The gene coding for the polyprotein (PP) of foot-and-mouth disease virus (FMDV)was obtained by PCR from recombinant plasmid rpMD18-T/PP. The PCR product was digested with Xba I and Not I and inserted into the cloning site of the adenovirus shuttle vector pAdTrack-CMV, previously digested with the same enzymes. This recombinant shuttle plasmid was designated rpAd-CMV/PP.

Chelate-controlled synthesis of racemic ansa-zirconocenes.

The reaction of Zr[PhN(CH(2))(3)NPh]Cl(2)(THF)(2) (5) with lithium ansa-bis-indenyl reagents Li(2)[XBI](Et(2)O) (XBI = (1-indenyl)(2)SiMe(2) (SBI, 7a), (2-methyl-1-indenyl)(2)SiMe(2) (MSBI, 7b), (2-methyl-4,5-benz-1-indenyl)(2)SiMe(2) (MBSBI, 7c), (2-methyl-4-phenyl-1-indenyl)(2)SiMe(2) (MPSBI, 7d), and 1,2-(1-indenyl)(2)ethane (EBI, 7e)) affords rac-(XBI)Zr[PhN(CH(2))(3)NPh] (8a-e) in high yield. The meso isomers were not detected by (1)H NMR. X-ray crystallographic studies show that the Zr[PhN(CH(2))(3)NPh] rings in 5, 8a, 8c, and (C(5)H(5))(2)Zr[PhN(CH(2))(3)NPh] (10) adopt twist conformations that position the N-Ph groups on opposite sides of the N-Zr-N plane.

Synthesis of TiO(2) supported on activated carbon by MOCVD: operation parameters study.

The metallo-organic chemical vapor deposition (MOCVD) technique has been applied to the preparation of the photocatalyst titanium dioxide supported on activated carbon. The effects of various condition parameters such as carrier gas flow rate, source temperature and deposition temperature on the deposition rate were investigated. The maximum deposition rate of 8.