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Article
Activation of a Refolded, Berberine-specific, Single-chain Fv Fragment by Addition of Free Berberine
A single-chain variable fragment (scFv) specific for berberine was produced in Escherichia coli. The anti-berberine scFv gene was cloned from hybridoma 1D5-3B-7 producing the monoclonal antibody. The variable reg...
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Article
Temperature fluctuations and heat transfer in a fluidized-bed combustor of waste oil
Temperature fluctuations and heat transfer characteristics were investigated in a fluidized-bed combustor of 0.102 m ID and 2.5 m in height, which was designed for waste oil combustion. Effects of excess air (AE)...
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Article
Development of monoclonal antibody against isoquinoline alkaloid coptisine and its application for the screening of medicinal plants
In the development of immunoassay technique, the design of hapten containing a functional group suitable for protein conjugate is the key step for the preparation of antibodies against small molecules. Coptisi...
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Article
Promotion of CO2 hydrogénation to hydrocarbons in three-phase catalytic (Fe-Cu-K-Al) slurry reactors
A three-phase slurry reactor has been employed to increase the CO2 conversion and decrease the selectivity of CO in the direct hydrogénation of CO2 to hydrocarbons, as it is beneficial for removal of the heat gen...
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Article
Decomposition characteristics of residue from the pyrolysis of polystyrene waste in a fluidized-bed reactor
Effective treatment of residue generated from the pyrolysis of polystyrene wastes has been one of the important factors in the recovery of styrene monomer and oil from polystyrene wastes. Depending on the expe...
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Article
Hydrogenation of CO2 over Fe-K based catalysts in a fixed bed reactors at elevated pressure
Catalytic hydrogenation of CO2to produce hydrocarbons was conducted in a fixed bed reactor (1.6 cm-IDx60 cm-High). Fe-K based catalysts (KRICAT-A, B) were used for more than 850 hours to maintain CO2 conversion l...
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Article
Characteristics of carbon dioxide hydrogenation in a fluidized bed reactor
Characteristics of CO2 hydrogenation were investigated in a fluidized bed reactor (0.052 m IDxl.5 m in height). Coprecipitated Fe-Cu-K-Al catalyst (dρ=75–90 Μm) was used as a fluidized solid phase. It was found t...