| Literature DB >> 29016652 |
Zhongwei Li1, Xiang Yuan1, Xuerong Cui1, Xin Liu1, Leiquan Wang1, Weishan Zhang1, Qinghua Lu1, Hu Zhu2.
Abstract
Welan gum is a kind of novel microbial polysaccharide, which is widely produced during the process of microbial growth and metabolism in different external conditions. Welan gum can be used as the thickener, suspending agent, emulsifier, stabilizer, lubricant, film-forming agent and adhesive usage in agriculture. In recent years, finding optimal experimental conditions to maximize the production is paid growing attentions. In this work, a hybrid computational method is proposed to optimize experimental conditions for producing Welan gum with data collected from experiments records. Support Vector Regression (SVR) is used to model the relationship between Welan gum production and experimental conditions, and then adaptive Genetic Algorithm (AGA, for short) is applied to search optimized experimental conditions. As results, a mathematic model of predicting production of Welan gum from experimental conditions is obtained, which achieves accuracy rate 88.36%. As well, a class of optimized experimental conditions is predicted for producing Welan gum 31.65g/L. Comparing the best result in chemical experiment 30.63g/L, the predicted production improves it by 3.3%. The results provide potential optimal experimental conditions to improve the production of Welan gum.Entities:
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Year: 2017 PMID: 29016652 PMCID: PMC5633192 DOI: 10.1371/journal.pone.0185942
Source DB: PubMed Journal: PLoS One ISSN: 1932-6203 Impact factor: 3.240
Fig 1Main work flow chart.
Sample data before normalization.
| glucose (g/L) | yeast (g/L) | KH2PO4 (g/L) | MgSO4 (g/L) | liquid volume (ml) | PH value | temperature (°C) | rotational speed(rpm) | inoculation amount | production (g/L) | |
|---|---|---|---|---|---|---|---|---|---|---|
| 1 | 40 | 2 | 5 | 0.1 | 50 | 10 | 28 | 150 | 5 | 0.9084 |
| 2 | 40 | 2 | 5 | 0.1 | 50 | 2 | 28 | 150 | 5 | 1.1484 |
| 3 | 40 | 2 | 5 | 0.1 | 50 | 3 | 28 | 150 | 5 | 1.6588 |
| 4 | 40 | 2 | 5 | 0.1 | 50 | 9 | 28 | 150 | 5 | 1.914 |
| 5 | 40 | 2 | 5 | 0.1 | 50 | 4 | 28 | 150 | 5 | 2.9348 |
| 6 | 60 | 10 | 5 | 0.1 | 50 | 7 | 32.5 | 175 | 5 | 3.08 |
| 7 | 40 | 2 | 5 | 0.1 | 50 | 5 | 28 | 150 | 5 | 4.0832 |
| 8 | 40 | 2 | 5 | 0.1 | 50 | 5.5 | 28 | 150 | 5 | 4.5936 |
| 9 | 40 | 2 | 5 | 0.1 | 50 | 8 | 28 | 150 | 5 | 6.2496 |
| 10 | 60 | 9 | 5 | 0.1 | 50 | 7 | 32.5 | 175 | 5 | 6.29 |
| 11 | 10 | 2 | 5 | 0.1 | 50 | 7 | 32.5 | 175 | 5 | 6.75 |
| 12 | 40 | 2 | 5 | 0.1 | 50 | 6 | 28 | 150 | 5 | 8.1664 |
| 13 | 60 | 8 | 5 | 0.1 | 50 | 7 | 32.5 | 175 | 5 | 8.7 |
| 14 | 20 | 2 | 5 | 0.1 | 50 | 7 | 32.5 | 175 | 5 | 9.23 |
| 15 | 40 | 2 | 5 | 0.1 | 50 | 6.8 | 28 | 150 | 1 | 10.73 |
| 16 | 40 | 2 | 5 | 0.1 | 50 | 7.5 | 28 | 150 | 5 | 10.9084 |
| 17 | 40 | 2 | 5 | 0.1 | 50 | 6.8 | 28 | 150 | 10 | 11.52 |
| 18 | 40 | 2 | 5 | 0.1 | 50 | 6.8 | 28 | 150 | 8 | 12.05 |
| 19 | 40 | 2 | 5 | 0.1 | 50 | 6.8 | 28 | 150 | 7 | 12.28 |
| 20 | 40 | 2 | 5 | 0.1 | 50 | 6.8 | 28 | 150 | 3 | 12.68 |
| 21 | 60 | 1 | 5 | 0.1 | 50 | 7 | 32.5 | 175 | 5 | 12.8 |
| 22 | 40 | 2 | 5 | 0.1 | 50 | 7 | 32.5 | 125 | 5 | 12.982 |
| 23 | 40 | 2 | 5 | 0.1 | 50 | 6.8 | 28 | 150 | 6 | 13.45 |
| 24 | 40 | 2 | 5 | 0.1 | 50 | 6.5 | 28 | 150 | 5 | 14.036 |
| 25 | 60 | 7 | 5 | 0.1 | 50 | 7 | 32.5 | 175 | 5 | 14.31 |
Sample data after normalization.
| glucose (g/L) | yeast (g/L) | KH2PO4 (g/L) | MgSO4 (g/L) | liquid volume (ml) | PH value | temperature (°C) | rotational speed(rpm) | inoculation amount | production (g/L) | |
|---|---|---|---|---|---|---|---|---|---|---|
| 1 | 0.375 | 0.1111 | 1 | 0 | 0.25 | 1 | 0.3 | 0.25 | 0.4444 | 0 |
| 2 | 0.375 | 0.1111 | 1 | 0 | 0.25 | 0 | 0.3 | 0.25 | 0.4444 | 0.005777 |
| 3 | 0.375 | 0.1111 | 1 | 0 | 0.25 | 0.125 | 0.3 | 0.25 | 0.4444 | 0.018064 |
| 4 | 0.375 | 0.1111 | 1 | 0 | 0.25 | 0.875 | 0.3 | 0.25 | 0.4444 | 0.024207 |
| 5 | 0.375 | 0.1111 | 1 | 0 | 0.25 | 0.25 | 0.3 | 0.25 | 0.4444 | 0.04878 |
| 6 | 0.625 | 1 | 1 | 0 | 0.25 | 0.625 | 0.75 | 0.5 | 0.4444 | 0.052275 |
| 7 | 0.375 | 0.1111 | 1 | 0 | 0.25 | 0.375 | 0.3 | 0.25 | 0.4444 | 0.076425 |
| 8 | 0.375 | 0.1111 | 1 | 0 | 0.25 | 0.4375 | 0.3 | 0.25 | 0.4444 | 0.088711 |
| 9 | 0.375 | 0.1111 | 1 | 0 | 0.25 | 0.75 | 0.3 | 0.25 | 0.4444 | 0.128575 |
| 10 | 0.625 | 0.8889 | 1 | 0 | 0.25 | 0.625 | 0.75 | 0.5 | 0.4444 | 0.129547 |
| 11 | 0 | 0.1111 | 1 | 0 | 0.25 | 0.625 | 0.75 | 0.5 | 0.4444 | 0.14062 |
| 12 | 0.375 | 0.1111 | 1 | 0 | 0.25 | 0.5 | 0.3 | 0.25 | 0.4444 | 0.174716 |
| 13 | 0.625 | 0.7778 | 1 | 0 | 0.25 | 0.625 | 0.75 | 0.5 | 0.4444 | 0.187561 |
| 14 | 0.125 | 0.1111 | 1 | 0 | 0.25 | 0.625 | 0.75 | 0.5 | 0.4444 | 0.20032 |
| 15 | 0.375 | 0.1111 | 1 | 0 | 0.25 | 0.6 | 0.3 | 0.25 | 0 | 0.236428 |
| 16 | 0.375 | 0.1111 | 1 | 0 | 0.25 | 0.6875 | 0.3 | 0.25 | 0.4444 | 0.240723 |
| 17 | 0.375 | 0.1111 | 1 | 0 | 0.25 | 0.6 | 0.3 | 0.25 | 1 | 0.255445 |
| 18 | 0.375 | 0.1111 | 1 | 0 | 0.25 | 0.6 | 0.3 | 0.25 | 0.7778 | 0.268203 |
| 19 | 0.375 | 0.1111 | 1 | 0 | 0.25 | 0.6 | 0.3 | 0.25 | 0.6667 | 0.27374 |
| 20 | 0.375 | 0.1111 | 1 | 0 | 0.25 | 0.6 | 0.3 | 0.25 | 0.2222 | 0.283369 |
| 21 | 0.625 | 0 | 1 | 0 | 0.25 | 0.625 | 0.75 | 0.5 | 0.4444 | 0.286258 |
| 22 | 0.375 | 0.1111 | 1 | 0 | 0.25 | 0.625 | 0.75 | 0 | 0.4444 | 0.290639 |
| 23 | 0.375 | 0.1111 | 1 | 0 | 0.25 | 0.6 | 0.3 | 0.25 | 0.5556 | 0.301905 |
| 24 | 0.375 | 0.1111 | 1 | 0 | 0.25 | 0.5625 | 0.3 | 0.25 | 0.4444 | 0.316011 |
| 25 | 0.625 | 0.6667 | 1 | 0 | 0.25 | 0.625 | 0.75 | 0.5 | 0.4444 | 0.322607 |
Fig 2SVR parameter selection result[GridSearchMethod].
Fig 3Comparison of raw data and regression predictive data.
Fig 4Relative error plot.
Fig 5The optimization result.
Fig 6The average maximum yield result graph under 500 iterations.
The optimal medium composition ratio.
| glucose (g/L) | yeast (g/L) | KH2PO4 (g/L) | MgSO4 (g/L) | liquid volume (ml) | PH value | temperature (°C) | rotational speed(rpm) | inoculation amount |
|---|---|---|---|---|---|---|---|---|
| 55.26 | 2.89 | 5.23 | 0.1 | 49.8 | 7.01 | 32.53 | 177.51 | 5 |