Sensors for biosensors: a novel tandem monitoring in a droplet towards efficient screening of robust design and optimal operating conditions

The Analyst ◽  
2019 ◽  
Vol 144 (8) ◽  
pp. 2511-2522 ◽  
Author(s):  
Daria Semenova ◽  
Yuliya E. Silina ◽  
Marcus Koch ◽  
Laura Micheli ◽  
Alexandr Zubov ◽  
...  
Keyword(s):  
Robust Design ◽  
Operating Conditions ◽  
Line Detection ◽  
Optimal Operating ◽  
System Parameters ◽  
Biosensor System ◽  
On Line ◽  
Efficient Screening

Development of a tandem monitoring approach that allows the simultaneous on-line detection of multiple biosensor system parameters.

A Graphical Approach for Assessing Optimal Operating Conditions in Robust Design

2009 ◽  
Vol 6 (3) ◽  
pp. 235-253 ◽  
Author(s):  
Anu A. Abraham ◽  
Timothy J. Robinson ◽  
Christine M. Anderson-Cook
Keyword(s):  
Robust Design ◽  
Operating Conditions ◽  
Optimal Operating ◽  
Graphical Approach

Development of Glucose On-line Detection System for Fermentation Process

2013 ◽  
Vol 40 (12) ◽  
pp. 1945-1949
Author(s):  
Xue-Jin GAO ◽  
Guang-Sheng LIU ◽  
Li CHENG ◽  
Ling-Xiao GENG ◽  
Ji-Xing XUE ◽  
...  
Keyword(s):  
Fermentation Process ◽  
Detection System ◽  
Line Detection ◽  
On Line

Validation of On-line Respiration Meter and its Applications by Computer Simulation

1992 ◽  
Vol 26 (5-6) ◽  
pp. 1355-1363 ◽  
Author(s):  
C-W. Kim ◽  
H. Spanjers ◽  
A. Klapwijk
Keyword(s):  
Steady State ◽  
Activated Sludge ◽  
Respiration Rate ◽  
Oxygen Demand ◽  
Operating Conditions ◽  
Mass Balances ◽  
Short Term ◽  
Respiration Rates ◽  
On Line ◽  
Made In

An on-line respiration meter is presented to monitor three types of respiration rates of activated sludge and to calculate effluent and influent short term biochemical oxygen demand (BODst) in the continuous activated sludge process. This work is to verify if the calculated BODst is reliable and the assumptions made in the course of developing the proposed procedure were acceptable. A mathematical model and a dynamic simulation program are written for an activated sludge model plant along with the respiration meter based on mass balances of BODst and DO. The simulation results show that the three types of respiration rate reach steady state within 15 minutes under reasonable operating conditions. As long as the respiration rate reaches steady state the proposed procedure calculates the respiration rate that is equal to the simulated. Under constant and dynamic BODst loading, the proposed procedure is capable of calculating the effluent and influent BODst with reasonable accuracy.

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