A methodology for scaling up continuous reactors using a Phenomenological-Based Semiphysical Model (PBSM) of the process is presented. First, a review of the most popular scale-up methods is made, finding that these methods do not guarantee an adequate commercial unit design and that a PBSM is a fundamental tool when scaling up chemical reactors. Taking into account these facts, a novel methodology is presented in which a process PBSM and its Hankel matrix are used for analysing the process dynamic behaviour and scaling it up, including the effect of the design variables over each state variable. Finally, the proposed methodology is applied to a polymerization reactor, comparing the scaled unit design when using this approximation and a tra...
This work presents a general model-based methodology to scale-up fed-batch bioprocesses. The idea be...
This work presents a general model-based methodology to scale-up fed-batch bioprocesses. The idea be...
This work presents a general model-based methodology to scale-up fed-batch bioprocesses. The idea be...
This work presents a methodology for scaling up Batch Processes (BPs). First, a review of the most p...
This work presents a methodology for scaling up batch processes (BPs). First, the most popular scale...
A review. Scale-up and/or scale-down procedures are crucial during the development of chem. processe...
The scale-up/-down of polymn. reactors has to deal with large viscosity changes during the process, ...
A rigorous dynamic model of the high-pressure polymerization of ethylene in tubular reactors is pres...
Process scale-up studies are, generally, non-linear. This basically means that it is not possible to...
Process scale-up studies are, generally, non-linear. This basically means that it is not possible to...
The classical scale-up approach for hydrogenation reaction processes usually includes numerous labor...
The classical scale-up approach for hydrogenation reaction processes usually includes numerous labor...
We present a method for the adjustment of parameters in the mathematical modeling of industrial tubu...
The classical scale-up approach for hydrogenation reaction processes usually includes numerous labor...
This work presents a general model-based methodology to scale-up fed-batch bioprocesses. The idea be...
This work presents a general model-based methodology to scale-up fed-batch bioprocesses. The idea be...
This work presents a general model-based methodology to scale-up fed-batch bioprocesses. The idea be...
This work presents a general model-based methodology to scale-up fed-batch bioprocesses. The idea be...
This work presents a methodology for scaling up Batch Processes (BPs). First, a review of the most p...
This work presents a methodology for scaling up batch processes (BPs). First, the most popular scale...
A review. Scale-up and/or scale-down procedures are crucial during the development of chem. processe...
The scale-up/-down of polymn. reactors has to deal with large viscosity changes during the process, ...
A rigorous dynamic model of the high-pressure polymerization of ethylene in tubular reactors is pres...
Process scale-up studies are, generally, non-linear. This basically means that it is not possible to...
Process scale-up studies are, generally, non-linear. This basically means that it is not possible to...
The classical scale-up approach for hydrogenation reaction processes usually includes numerous labor...
The classical scale-up approach for hydrogenation reaction processes usually includes numerous labor...
We present a method for the adjustment of parameters in the mathematical modeling of industrial tubu...
The classical scale-up approach for hydrogenation reaction processes usually includes numerous labor...
This work presents a general model-based methodology to scale-up fed-batch bioprocesses. The idea be...
This work presents a general model-based methodology to scale-up fed-batch bioprocesses. The idea be...
This work presents a general model-based methodology to scale-up fed-batch bioprocesses. The idea be...
This work presents a general model-based methodology to scale-up fed-batch bioprocesses. The idea be...