The kinetic parameters of anaerobic propionate degradation by biomass from 7 continuously stirred tank reactors differing in temperature, hydraulic retention time and substrate composition were investigated. In substrate‐depletion experiments (batch) the maximum propionate degradation rate, A max, and the ...
Alvarez-Ramirez, J (1999) Robust PI stabilization of a class of continuously stirred-tank reactors. AIChE J 45: pp. 1992-2000Robust PI Stabilization of a Class of Continuously Stirred-Tank - Ramirez - 1999Ramirez, J. A. "Robust PI Stabilization of a Class of Continuously Stirred-Tank ...
This study presents the thermochemical energy storage as a new continuously stirred tank three-phase suspension reactor for storing heat from renewable sources or waste heat with almost no losses, in reaction. Therefore, the reactor was built of glass, where process parameters, such as the mean ...
For the production of OAs, dark fermentation processes were carried out for treated SCW, CCWP and ADB in continuously stirred tank reactors (CSTR (Tecnovetro, Monza, Italy), working volume: 1.5 L, agitation: 200 rpm) to reach a fast sugar fermentation under anaerobic and thermophilic conditions...
aIn general, powder experiments measure a bulk dissolution rate by changes in solution composition. These changes can be observed as a function of time (free drift) or flow (singlepass plug flow reactors, fluidized bed reactors, continuously stirred tank reactors, and variants thereof) 一般来说,...
To improve the performance of anaerobic digestion, as well as for flexible biogas production, the effects of different feeding regimes on biogas production, system stability, and microbial community structure were investigated using laboratory-scale semi-continuously stirred tank reactors (semi-CSTRs) ...
series of continuously stirred tank reactors and, in the first tank, adding air to the solution; heating the solution to an elevated temperature; recycling a portion of selectively precipitated ferric arsenate compounds to the said first tank; and seeding the solution with ferric arsenate compounds....
Section > Chapter Heyse, E.; Dai, D.; Rao, P.S.resh C.; Delfino, J.J. Journal of Contaminant Hydrology 25(3-4): 337-355 1997 ISSN/ISBN:0169-7722 10.1016/s0169-7722(96)00043-5 003091844 Article emailed within 0-6 h Buy Now for$19.90 ...
example ejectors or mechanical stirring means, like for example impellers. Such reactors may be of the so-called bubble column slurry type reactor and mechanically agitated stirred tank reactor. In a preferred embodiment the reactor is a continuously operated stirred reactor wherein carbon dioxide and...
supplied to a first slurry tank. Here, the aromatic dicarboxylic acid is quantified in a hopper and input into the first slurry tank. Here, while the internal temperature of the first slurry tank is maintained in a range from about 70 to about 80° C., the aliphatic oligomer is stirred....