Characterization of reactors

Microstructural Characterization of Reactor Pressure Vessel Steels Post-Irradiation Annealing Experiments Joint EPRI-CRIEPI RPV Embrittlement Studies (1999-2004), Electric Power Research Institute, Palo Alto, CA, 2004, 1003531, and CRIEPI, Tokyo, Japan, Q980401. 

Polymerization reactions. Polymers are characterized by the distribution of molecular w eight about the mean as well as by the mean itself. The breadth of this distribution depends on whether a batch or plug-flow reactor is used on the one hand or a continuous well-mixed reactor on the other. The breadth has an important influence on the mechanical and other properties of the polymer, and this is an important factor in the choice of reactor. 

Table I provides an overview of general reactor designs used with PS and HIPS processes on the basis of reactor function. The polymer concentrations characterizing the mass polymerizations are approximate there could be some overlapping of agitator types with solids level beyond that shown in the tcd>le. Polymer concentration limits on HIPS will be lower because of increased viscosity. There are also additional applications. Tubular reactors, for example, in effect, often exist as the transfer lines between reactors and in external circulating loops associated with continuous reactors.

The authors wish to acknowledge the contributions of Jeff L. Haris, Robert K. Sato, and Dianna O. Durieux for their work in characterizing the reactor effluent streams in the contaminant studies. 

In this paper, TiCU was oxidized in the flow reactor at various temperature and gas flow rate. The wall scales were characterized by scan electron microscopy and X-ray diffraction. The effects of reactor wall surface state, radial growth of scale layer and reactor axial temperature distribution on scaling formation were discussed. At the same time, the mechanism of scaling on the reactor wall was explored furthermore. 

Characterization of a Zeoiite Membrane for Catalytic Membrane Reactor Application... 

A detailed characterization of micro mixing and reaction performance (combined mixing and heat transfer) for various small-scale compact heat exchanger chemical reactors has been reported [27]. The superior performance, i.e. the process intensification, of these devices is evidenced and the devices themselves are benchmarked to each other. 

Losey, M. W, Schmidt, M. A., Jensen, K. F., Microfabricated multiphase packed-bed reactors characterization of mass transfer and reactions, Ind. Chem. Res. 

Furan was dimethoxylated to give 2,5-dihydro-2,5-dimethoxyfuran, using electrogenerated bromine molecules generated from bromide salts in electrolyte solutions [71]. This reaction was characterized in classical electrochemical reactors such as pump cells, packed bipolar cells and solid polymer electrolyte cells. In the last type of reactor, no bromide salt or electrolyte was used rather, the furan was oxidized directly at the anode. H owever, high consumption of the order of 5-9 kWh kg (at 8-20 V cell voltage) was needed to reach a current efficiency of 75%. 

A hydrodynamic characterization of the micro reactor is given in [12], A flow-pattem map reveals the existence of dispersed flow, annular flow, slug-dispersed... 

The thiol was obtained in >98% yield with trace amounts of the disulfide at 175°C and 700 psig H2 reactor pressnre in 1.5 honrs at a 900 1 substrate catalyst molar ratio. As discussed above, it is known that palladinm and other groups 8 to 10 metal catalysts are poisoned by the prodnct thiol, traces of hydrogen sulfide byproduct, and hydrogen cyanide coprodnct (6), bnt it is surprising that this catalyst is so robnst The effects of solvents, temperature, pressure, catalyst, and recycle will be discnssed. The characterization of the catalyst by various techniques will help to explain some of these observations. 

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