A8 - Apical and basolateral flow rate influence intestinal absorption in fresh intestinal tissue inside a novel intestine on a chip model

2020 ◽  
Vol 35 (1) ◽  
pp. S20-S21
Author(s):  
Hossein Eslami Amirabadi ◽  
Joline Boogaard ◽  
Esmée Wierenga ◽  
Tim Donkers ◽  
Mariska Grölers-Mulderij ◽  
...  
Keyword(s):  
Intestinal Absorption ◽  
Flow Rate ◽  
Intestinal Tissue ◽  
Flow Rate Influence

A Sensitive Medium-Throughput Method to Predict Intestinal Absorption in Humans Using Rat Intestinal Tissue Segments

2015 ◽  
Vol 104 (9) ◽  
pp. 2807-2812 ◽  
Author(s):  
Laís Cristina Da Silva ◽  
Taynara Lourenço Da Silva ◽  
Alisson Henrique Antunes ◽  
Kênnia Rocha Rezende
Keyword(s):  
Intestinal Absorption ◽  
Intestinal Tissue

scholarly journals Flow rate influence of the peristaltic-based pumps on the QCM sensor

2020 ◽  
Vol 1465 ◽  
pp. 012003
Author(s):  
R A Pratiwi ◽  
M A Akbar ◽  
S P Sakti
Keyword(s):  
Flow Rate ◽  
Flow Rate Influence

scholarly journals The Flow Rate Influence on the Interaction of a Radial Pump Impeller and the Diffuser

2004 ◽  
Vol 10 (4) ◽  
pp. 309-317
Author(s):  
A. Akhras ◽  
M. Hajem ◽  
J.-Y. Champagne ◽  
R. Morel
Keyword(s):  
Flow Rate ◽  
Pump Impeller ◽  
Radial Pump ◽  
Flow Rate Influence

scholarly journals Simulating Trambouze reaction for a series reactor

2020 ◽  
Vol 3 (1) ◽  
pp. 1
Author(s):  
Amizon Azizan ◽  
Nornizar Anuar
Keyword(s):  
Flow Rate ◽  
Coming Out ◽  
Flow Reactor ◽  
Plug Flow ◽  
Volumetric Flow Rate ◽  
Continuous Stirred Tank Reactor ◽  
Maximum Conversion ◽  
Outlet Stream ◽  
Continuous Stirred Tank ◽  
Flow Rate Influence

Simulating the existing data on Trambouze reaction is compiled in this article. The objective of the work is to present the change of volumetric flow rate and the inlet concentration of key reactant A in a series continuous stirred tank reactor-plug flow reactor (CSTR-PFR) configurations. The volumetric flow rate does not affect selectivity and conversion for a constant volumetric flow rate operating condition, entering CSTR and PFR, at a specific concentration of reactant. The CSTR-PFR series reactor configuration is proposed for the aim of maximizing the selectivity of the desired product B in comparison to the undesired products X and Y. CSTR as the first reactor is capable to achieve the maximum conversion at the highest selectivity of A. PFR is then proposed after CSTR in a configuration of CSTR-PFR, to allow higher conversion value to be achieved for the resulted outlet stream conditions coming out of the first reactor, CSTR. Both reactors commonly encounter a decrease in the initial concentration of A and an increase to the formation of other products. The CSTR entering volumetric flow rate influence the volume sizes needed in achieving the maximum selectivity and conversion

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