Control of bioreactor processes
Processes, as well as associated systems and computer program (software) products, are disclosed for the biological conversion of CO into desired end products such as ethanol. The control methodologies used for these processes can advantageously result in a reduced time required for a batch operation or other initial operating period, prior to achieving a continuous operation, which may be demarcated either by the addition of fresh culture medium at a defined flow rate or by another process initiation target. The control methodologies may alternatively, or in combination, improve a process performance parameter, such as productivity of the desired end product or bacterial growth rate, during this batch operation or other initial operating period.
1. A computer program implemented process for controlling a CO fermentation process in a bioreactor, when executed by a computer processor, performs the steps comprising:
i) the computer processor continuously receiving a CO-containing substrate flow rate from the bioreactor;
ii) continuously receiving a pH value of a culture medium contained within the bioreactor;
iii) continuously determining a basic neutralizing agent flow rate and a CO-containing substrate flow rate to the bioreactor using the equation:
W *BIOPROD+ X *METPROD=NEUTFLO= Y *COFLO+ Z
wherein BIOPROD is the bacteria productivity, METPROD is the acetic acid productivity, NEUTFLO is the flow rate of the basic neutralizing agent, COFLO is the flow rate of the CO-containing substrate and W, X, Y, and Z are factors previously determined using linear regression analysis, by the computer processor, using the bacteria concentration and acetic acid concentration at successive time intervals;
iv) maintaining the pH of the culture medium at a predetermined set point by adjusting the CO-containing substrate flow rate to the bioreactor based on the determined CO-containing substrate flow rate; and
adjusting the neutralizing agent flow rate to the bioreactor based on the determined neutralizing agent flow rate.
2. A system comprising:
a) a bioreactor,
b) a vessel, configured as a source of a basic neutralizing agent;
c) a first controller in communication with the bioreactor, a computer, and the vessel and configured to control a basic neutralizing agent flow rate based on receiving a signal from the computer;
d) the first controller comprising a basic neutralizing agent flow rate sensor and configured to continuously send the basic neutralizing agent flow rate to the computer and further configured to control the basic neutralizing agent flow rate to the bioreactor based on receiving a signal from the computer;
e) a CO-containing substrate flow rate sensor in communication with the computer, the CO-containing substrate flow rate sensor configured to continuously send the CO-containing substrate flow rate to the computer;
f) the computer configured to continuously receive the CO-containing substrate flow rate;
g) the computer configured to calculate a basic neutralizing agent flow rate and sending the neutralizing agent flow rate to the first controller configured to adjust the basic neutralizing agent flow rate; and
h) the computer comprising a computer processor which executes a computer program implemented process for determining the basic neutralizing agent flow rate and the CO-containing substrate flow rate to the bioreactor using the equation:
W *BIOPROD+ X *METPROD=NEUTFLO= Y *COFLO+ Z
wherein BIOPROD is the bacteria productivity, METPROD is the acetic acid productivity, NEUTFLO is the flow rate of the basic neutralizing agent, COFLO is the flow rate of the CO-containing substrate and W, X, Y, and Z are factors previously determined using linear regression analysis, by the computer processor, using the bacteria concentration and acetic acid concentration at successive time intervals.