Multi-target Optimization in Glutamate Fermentation Introduction: The optimization of fermentation process in glutamate production is similar to the optimization of fermentation in penicillin production described elsewhere. However, this is a 4-target, 3-class and 14-dimensional optimization problem. Optimization Targets: There are four (4) targets that need to be optimized in the process. They are:Application Note Zaptron Systems, Inc.
1) Conversion rate (from glucose to glutamic acid) should be high
First segment - data from 0 to 12 hours | |
Second segment -data from 12 to 24 hours |
|
Third segment - data from longer than 24 hours (to the fermentation end) |
Some of data, including PH value, ventilation rate and temperature, were then averaged in each of the three segments to generate the averaged features for each segment. Data samples were further classified into 3 classes according to the range of features:
Class 1: the glucose-to-sugar conversion rate is larger than 50%, and the time period of fermentation is less than 34 hours. | |
Class 2: the glucose-to-sugar conversion rate is smaller than 49.5%, and the time period of fermentation is larger than 34.5 hours. | |
Class 3: samples have other parameters |
Feature Selection:
Features that have been selected by using MasterMiner include relevant operation parameters, such as temperature, ventilation, PH value, and etc., and the physical-chemical data (as time series data) of liquors, such as glucose concentration, OD value and etc. The OD is an optical property of sugar (for example glucose). Since a change in OD value indicates a change in substance concentration or composition, the OD vale is used as a parameter for monitoring the process.The complete set of features for the overall fermentation process is listed below:
x1 - transparency of liquor
# | X1 |
X2 |
X3 |
X4 |
X5 |
X6 |
X7 |
X8 |
X9 |
X10 |
X11 |
X12 |
X13 |
X14 |
1 | .37 | -.14 | .47 | -.09 | -.078 | -.11 | -.05 | -.24 | 24 | 20 | 18 | -.27 | 1.34 | .59 |
2 | .84 | -.13 | .30 | .03 | -.016 | .09 | -.04 | -.20 | 33 | 30 | 46 | .39 | 1.08 | .64 |
3 | .56 | -.01 | .18 | -.14 | -.026 | .01 | -.03 | -.12 | -3 | 6 | 71 | -.15 | .74 | .35 |
The above prediction value are roughly in agreement with the result obtained by another method whereby single features were adjusted to search for the best operational direction. However, some features, such as X2, are not in agreement in these two methods.
In addition, MasterMiner offered the following advisory to production:PH value should (in this concrete case) be slightly reduced | |
Temperature should be slightly increased. | |
Ventilation rate should be slightly increased. |
In real-world fermentation operations at the client site, the optimization of the four targets, i.e., conversion rate, productivity, yield, and fermentation period, has been achieved simultaneously by using the optimal samples obtained by MasterMiner. Results from 390 production batches (tanks) were averaged to give the following results:Results:
Conversion rate was increased by 2.90%, | |
Yield was increased by 2.56% | |
Productivity was increased by 1.45% | |
Saved glucose by 1.43%. | |
Profit generated: RMB 1,610,000 (or US $200,000) per year |
The model obtained by MasterMiner has since been used in production by the client with satisfactory results.
© Copyright, 1998-2000, Zaptron Systems, Inc. Back to Home.