Vacuum residue (VR) upgrading was conducted in the environment of supercritical water (SCW) without oxygen addition in an attempt to yield a maximum of light oil. Simulated distillation of the liquid products from a set of orthogonal experiments shows that temperature should not be too high to restrict coke formation, and the most beneficial condition is found at (1) 420 °C for the temperature, (2) 0.15 g/cm3 for the water density, (3) 2 g/g for the H2O/oil ratio, and (4) 1 h for the reaction time. A simultaneous increase of the water density and H2O/oil would significantly improve the cracking behavior and the yield in light oil. Scattered coke particles between 10 and 100 μm were generated from VR cracking, which suggests the dispersion effect of SCW. The infrared spectrum analysis has indicated an increase in the H/C atomic ratio in the liquid product, which implies that hydrogen is generated from the condensation reactions rather than from water because no oxygen-containing group was detected.

For the accurate identification of medicinal licorice species, nucleotide sequences of four types of DNA regions were researched for 205 specimens, including three species used as licorice: Glycyrrhiza uralensis, Glycyrrhiza glabra, and Glycyrrhiza inflata. The four DNA regions were the internal transcribed spacer (ITS) on nuclear ribosomal DNA, the rbcL gene, the matK gene, and the trnH-psbA intergenic region on chloroplast DNA (cpDNA). Ten genotypes were consequently recognized as combinations of the sequence data obtained from the four DNA regions. Species-specific genotypes were defined from the frequency of the appearance of species in each genotype and from the phylogenetic relationships of the 10 genotypes. This revealed the possibility of identifying licorice species based on the 10 genotypes. Next, comparison of species identifications by each DNA region suggested that efficient identification of licorice species is possible using the genetic information obtained from the ITS and trnH-psbA intergenic region. Additionally, concerning the phylogenetic relationships of the Glycyrrhiza species used as licorice, it is suggested from the genetic information of the four types of DNA regions that G. glabra is more closely related to G. inflata than to G. uralensis. In the G. uralensis examined, four genotypes were recognized as intra specific variations. The appearance frequency of each genotype in G. uralensis differed according to the area in China. G. uralensis may have expanded its distribution areas from western to eastern China because many licorices with the phylogenetic ancestral genotype were observed in western areas, while many with the derivative genotype were observed in eastern areas.

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The reaction kinetics of the pyrolysis of heavy oil in the presence of supercritical water (SCW) and high pressure N 2 were measured. At any reaction temperature applied, the pyrolysis under SCW environments is faster than that under N 2 environments. Meanwhile, at lower temperatures the pyrolysis under both environments is accelerated by the introduction of coke into the feedstock. On the basis of a first-order four-lump reaction network consisting of the sequential condensation of maltenes and asphaltenes, the pyrolysis in whichever medium can be preferably described either by the lumped reaction kinetic model modified with autocatalysis and pseudoequilibrium or by the model modified solely with pseudoequilibrium. Benefited from the reduced limitation of diffusion to reaction kinetics, the pyrolysis in the SCW phase is more sensitive to the increase in reaction temperature than that in the oil phase, disengaging readily from the dependence on autocatalysis at a lower temperature.

In the presence of supercritical water (SCW) and N 2 , the pyrolysis of heavy oil was investigated to distinguish the difference in the reaction kinetics between the upgrading in the SCW and oil phases. The pyrolysis in the SCW phase is faster than that in the oil phase, but the reaction in whichever phase is retarded by vigorous stirring. The pyrolysis can be preferably described by a four-lump kinetic model consisting of the condensation of maltenes and asphaltenes in series. In the SCW phase, highly dispersed asphaltenes are isolated by water clusters from maltenes dissolved in SCW surroundings, by which the condensation of asphaltenes is drastically accelerated. Benefited from excellent mass transfer environments in SCW, the condensation of maltenes is promoted simultaneously. The introduction of SCW into the pyrolysis of heavy oil results in an effectively increased upgrading efficiency, but its influence on the properties of equilibrium liquid products is minor.

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