| Literature DB >> 32195298 |
Deokyeol Jeong1, Suji Ye1, Heeyoung Park1, Soo Rin Kim1.
Abstract
Saccharomyces cerevisiae expressing heterologous pathways for xylose, arabinose, and galacturonic acid metabolism has been constructed by a Cas9-based genome editing technology [1]. The fermentation performance of the final strain (YE9) was tested under various substrate conditions, and the fermentation parameters were calculated. The dataset can be used for designing bioprocesses for pectin-rich biomass.Entities:
Keywords: Bioethanol; CRISPR/Cas9; Citrus peel waste; Metabolic engineering; Pectin; Sugar beet pulp
Year: 2020 PMID: 32195298 PMCID: PMC7078300 DOI: 10.1016/j.dib.2020.105359
Source DB: PubMed Journal: Data Brief ISSN: 2352-3409
Fig. 1Fermentation profiles of the YE9 strain in a complex medium containing (A) 40 g/L d-glucose, (B) 40 g/L d-fructose, and (C) 40 g/L d-galactose as the sole carbon sources. Fermentations were performed under oxygen-limited conditions (130 rpm) with a starting cell density of 25 g/L. All experiments were performed in biological triplicate, and the error bars indicate the standard deviations.
Fermentation profiles of the native S. cerevisiae strain (D452-2) and engineered strain (YE9) expressing heterologous pathways for metabolizing d-xylose, l-arabinose, and d-galacturonic acid (galUA).
| Strain | Substrate | Substrate consumed (g/L) | Substrate consumption rate (g/L/h) | Products (g/L) | Parameters | |||||
|---|---|---|---|---|---|---|---|---|---|---|
| Glycerol | Ethanol | |||||||||
| D452-2 | D-xylose | 5.9 ± 0.2 | 0.19 ± 0.01 | 0.3 ± 0.0 | 0.07 ± 0.02 | |||||
| 1.3 ± 0.6 | 0.08 ± 0.03 | |||||||||
| galUA | < 0.0 | < 0.00 | ||||||||
| YE9 | 33.7 ± 0.5 | 1.41 ± 0.02 | 0.6 ± 0.1 | 11.3 ± 0.1 | 0.02 ± 0.00 | 0.34 ± 0.01 | 0.05 ± 0.00 | |||
| 30.2 ± 0.1 | 0.63 ± 0.07 | 1.9 ± 0.1 | 0.07 ± 0.00 | <0.00 | ||||||
| galUA | 6.7 ± 0.7 | 0.27 ± 0.01 | 0.3 ± 0.1 | 0.3 ± 0.0 | 0.04 ± 0.01 | 0.08 ± 0.02 | < 0.00 | |||
Fermentations were performed in a complex medium containing 40 g/L d-xylose, 40 g/L l-arabinose, or 20 g/L d-galacturonic acid under oxygen-limited conditions (130 rpm) with a starting cell density of 25 g/L. Substrate consumption rate was calculated for 24 h and the others were calculated for 72 h.
YGlycerol, glycerol yield (g glycerol/g substrate); YEthanol, ethanol yield (g ethanol/g substrate); PEthanol∗, specific ethanol productivity (g ethanol/g cell/h); n. d., not detected.
Fig. 2Effect of d-galacturonic acid on the rate of d-xylose consumption in the YE9 strain. Consumption rate of d-xylose (A) and d-galacturonic acid (B) was evaluated under 40 g/L D-xylose and different d-galacturonic acid concentrations (0–100 g/L). All experiments were performed in biological triplicate, and error bars indicate standard deviations and were not visible when smaller than the symbol size.
Fermentation profiles of mixed culture by engineered S. cerevisiae YE9 strain expressing heterologous pathways metabolizing d-xylose, l-arabinose, and d-galacturonic acid (galUA).
| Medium | Substrate consumed (g/L) | galUA consumption rate (g/L/h) | Products (g/L) | Parameters | |||||
|---|---|---|---|---|---|---|---|---|---|
| galUA | Sugars | Glycerol | Ethanol | ||||||
| galUA | 6.7 ± 0.7 | – | 0.27 ± 0.01 | 0.3 ± 0.1 | 0.3 ± 0.0 | 0.04 ± 0.01 | 0.08 ± 0.02 | < 0.00 | < 0.00 |
| galUA + Glucose | 3.3 ± 0.2 | 36.7 ± 0.1 | 0.14 ± 0.01 | 2.4 ± 0.3 | 16.9 ± 0.2 | 0.06 ± 0.01 | 0.40 ± 0.01 | 0.06 ± 0.00 | 0.66 ± 0.01 |
| galUA + Fructose | 4.5 ± 0.3 | 36.1 ± 0.8 | 0.18 ± 0.02 | 2.9 ± 0.1 | 16.9 ± 0.5 | 0.07 ± 0.00 | 0.36 ± 0.01 | < 0.00 | 0.65 ± 0.03 |
| galUA + Galactose | 4.6 ± 1.2 | 25.4 ± 7.3 | 0.17 ± 0.03 | 1.6 ± 0.7 | 2.4 ± 1.1 | 0.04 ± 0.01 | 0.05 ± 0.02 | < 0.00 | < 0.00 |
| galUA+ Xylose | 13.1 ± 0.4 | 33.3 ± 0.5 | 0.49 ± 0.02 | 4.5 ± 0.1 | 12.8 ± 0.3 | 0.08 ± 0.00 | 0.23 ± 0.01 | 0.01 ± 0.00 | 0.04 ± 0.00 |
| galUA+ Arabinose | 11.9 ± 0.7 | 28.4 ± 0.1 | 0.32 ± 0.03 | 4.2 ± 0.2 | 4.1 ± 0.5 | 0.11 ± 0.01 | 0.11 ± 0.02 | < 0.00 | < 0.00 |
| galUA | 15.3 ± 0.6 | 33.7 ± 0.1 (X) | 0.49 ± 0.04 | 5.3 ± 0.6 | 16.5 ± 1.2 | 0.07 ± 0.00 | 0.22 ± 0.01 | < 0.00 | 0.02 ± 0.00 |
Fermentations were performed in a complex medium containing 20 g/L d-galacturonic acid (galUA) and 40 g/L sugar (d-glucose, d-fructose, d-galactose, d-xylose, l-arabinose, and mixture of d-xylose and l-arabinose) under oxygen-limited conditions (130 rpm) with a starting cell density of 25 g/L. d-galacturonic acid consumption rate was calculated for 24 h and the others were calculated for 72 h.
YGlycerol, glycerol yield (g glycerol/g substrates); YEthanol, ethanol yield (g ethanol/g substrates); PGlycerol∗, specific glycerol productivity (g glycerol/g cell/h); PEthanol∗, specific ethanol productivity (g ethanol/g cell/h).
Fig.3Construction of engineered S. cerevisiae YE9 strains expressing heterologous d-xylose, d-galacturonic acid, and l-arabinose pathways. (A) Strain construction using Cas9-based in vivo assembly and genome integration strategy. (B) Confirmation primers for correct assembly and integration by yeast colony PCR. The primer sequences are listed in Table S5.
Saccharomyces cerevisiae strains used for the construction of YE9.
| Strains | Description/relevant genotype | Ref. |
|---|---|---|
| D452-2 | Wild type; | [ |
| DY02 | Expressing the heterologous | |
| YE3 | DY02 | |
| YE4 | DY02 | |
| YE5 | DY02 | |
| YE6 | Expressing the heterologous D-xylose and | |
| YE6 | YE6 | |
| YE6 | YE6 | |
| YE01 | Expressing the heterologous | [ |
| YE9 | Expressing the heterologous |
XYL1, XYL2, and XYL3 are derived from Pichia stipitis; gaaA, gaaC, and gaaD are derived from Aspergillus niger; lgd1 and lad1 are derived from Trichoderma reesei; alx1 is derived from Ambrosiozyma monospora.
Guide RNA (gRNA) plasmids.
| gRNA | Target cut site | gRNA and PAM sequences (5’-) | Plasmid name |
|---|---|---|---|
| ALD6.1 | GTCAAGATCACACTTCCAAA TGG | pRS42H-ALD6.1 | |
| PHO13.1 | TCCCTTATCTATTAACTTTC CGG | pRS42H-PHO13.1 | |
| YPR1.1 | CATGGTAGATTATTATCTGT GGG | pRS42H-YPR1.1 | |
| INT#4 | Intergenic region upstream | CTCTCGAAGTGGTCACGTGC GGG | pRS42H-INT#4 |
| INT#6 | Intergenic region upstream | TTGTCACAGTGTCACATCAG CGG | pRS42H-INT#6 |
| INT#7 | Intergenic region downstream | GATACTTATCATTAAGAAAA TGG | pRS42H-INT#7 |
Primers used for construction of guide RNA plasmids.
| Plasmid name | Primers | Sequences (5’-) |
|---|---|---|
| pRS42H-ALD6.1 | Kim044 | |
| Kim045 | ||
| pRS42H-PHO13.1 | Kim624 | |
| Kim625 | ||
| pRS42H-YPR1.1 | Kim535 | |
| Kim536 | ||
| pRS42H-INT#4 | Kim310 | |
| Kim311 | ||
| pRS42H-INT#6 | Kim314 | |
| Kim315 | ||
| pRS42H-INT#7 | Kim486 | |
| Kim487 |
Primers used for construction of donor DNA fragments.
| Template genomic DNA | Donor DNA fragments | Primers | Sequences (5’-) |
|---|---|---|---|
| Kim626 | |||
| SOO384 | |||
| SOO385 | |||
| SOO386 | AAT | ||
| SOO387 | GGA | ||
| SOO388 | ATTCTTTGAAGGTACTT | ||
| SOO389 | TTTTAAAGTTTACAAAT | ||
| SOO390 | CACCAA | ||
| SOO391 | AATTAT | ||
| SOO392 | AAAAAATTGAT | ||
| SOO393 | GTCAAGTGTCT | ||
| Kim627 | |||
| Kim628 | |||
| SOO374 | AA | ||
| SOO375 | AT | ||
| SOO376 | GCAACTA | ||
| SOO377 | CAAGATG | ||
| Kim629 | |||
| Kim379 | |||
| Kim380 | TCAACA | ||
| Kim381 | TCTGTC | ||
| Kim382 | TAGA | ||
| Kim383 | GGAT | ||
| Kim384 | |||
| Kim385 | |||
| Kim386 | |||
| Kim387 | |||
| Kim388 | ATTGATCTAT | ||
| Kim389 | CTGCCCATCT | ||
| Kim390 | |||
| Kim391 | |||
| Kim392 | GACTCCGGGGCG | ||
| Kim393 | TTCGAATA | ||
| Kim394 | ATTTAAAT | ||
| Kim395 | TGAGAAGT | ||
| Kim396 | |||
| Kim410 | |||
| Kim411 | TAGTTC | ||
| Kim412 | AGCCAA | ||
| Kim413 | AAACTCGAA | ||
| Kim414 | TATTATTTT | ||
| Kim415 | |||
| Kim553 | |||
| Kim554 | |||
| Kim537 | |||
| Kim538 | |||
| Kim541 | |||
| Kim542 | TA | ||
| Kim543 | TC | ||
| Kim544 | GT | ||
| Kim545 | TG | ||
| Kim546 | |||
The flanking region is underlined.
Saccharomyces cerevisiae D452-2; Pichia stipitis CBS 6054; Aspergillus niger CBS 120.49; Trichoderma reesei ATCC 5676.
Primers used for confirmation of correct assembly and integration.
| Primers | Sequences (5’-) | Primers | Sequences (5’-) |
|---|---|---|---|
| Introduction of | Introduction of | ||
| Kim049 | GGAACGGTGAGTGCAACG | Kim322 | GCGCATCTATTTGCCGTC |
| Kim427 | AAACTGTTCACCCAGACACC | Kim397 | GCTGGGGGAGCCATTTTTTATTG |
| Kim194 | AGCGCAACTACAGAGAACAGG | Kim398 | GTGGGAGCTGAAGTAGACTTAG |
| Kim100 | CGGCACCGTCGAACAATCTG | Kim323 | TCACGACACACCTCACTG |
| Kim101 | CCGCTTACTCTTCGTTCGGTCC | Kim399 | CCTGTGATGGTGACTTCAGAC |
| Kim193 | CTCAGCATCCACAATGTATCAG | Kim401 | GAACGGAGAGAAGATCTGAATTG |
| Kim426 | GCGCTATTGCATTGTTCTTGTC | Kim400 | ACAGCCTGTTCTCACACAC |
| Kim547 | AGGTATGCGATAGTTCCTCAC | Kim402 | GCGGGGTAAAAGGCATTTTTTTTG |
| Kim125 | TGCAGCTTCCAATTTCGTCAC | Kim408 | GCCGGATATTGCTTAGGTG |
| Kim630 | GAGGTGACACCCTTACCAAC | ||
| Kim631 | CTGCTACTCACACCTTCAACTC | ||
| Kim632 | CGCTGAACCCGAACATAGAAATATC | Kim490 | GGCACTAGGAGCATTTGTCG |
| Kim633 | TCGATATTTCTATGTTCGGGTTCAG | Kim304 | GCTTCGCTAATCCAGAGGTC |
| Kim078 | GATTGGAATTGGTTCGCAGTG | Kim400 | ACAGCCTGTTCTCACACAC |
| Kim048 | GAGGAAGACGTTGAAGGTGG | Kim491 | GTCCCTTAGGGTGCGTATAATG |
| Kim149 | TTTGAAGTGGTACGGCGATG | ||
| Kim577 | CACCCAAGCACAGCATAC | ||
| Kim634 | TGGCTCGATAACGAAGATTCAG | Kim539 | CAATTCCGTGAAACCCTTTTCTT |
| Kim635 | GTCTTGTAGATTGAGAACTGGTCC | Kim540 | CTGCCAACTTCTTCTTCATTCAA |
| Kim636 | TCTATGAGGCAAGTAAGAGGCAC | ||
| Kim492 | AACAGGCGACAGTCCAAATG | ||
| Kim077 | TTGGAGTTCAAACTGGCGAG | Kim326 | GGTTCTGACTCCTACTGAGC |
| Kim093 | GCAAAGATAGCGGCGTAGGTG | ||
| Kim549 | GCATCCTTTGCCTCCGTTC | ||
| Kim327 | AGCATCGAGTACGGCAGTTC | ||
Chemical composition of pectin-rich biomass.
| Source | Arabinose | Galacturonic acid | Ratio | Reference |
|---|---|---|---|---|
| Orange peel hydrolysate (g/L, ∼ 10% solid loading) | 32.6 | 13.2 | 2.47 | [ |
| Sugar beet pulp hydrolysate (g/100 g dry matter) | 22.5 | 22.5 | 1.00 | [ |
Specifications Table
| Subject | Applied Microbiology and Biotechnology |
| Specific subject area | Yeast metabolic engineering |
| Type of data | Tables and Figures |
| How data were acquired | The fermentation data were obtained by HPLC (Agilent Technologies 1260 series). |
| Data format | Raw and Analysed |
| Parameters for data collection | Fermentation conditions at 30oC and 130 rpm. |
| Description of data collection | Time series analysis of fermentation samples. |
| Data source location | Institution: Kyungpook National University |
| Data accessibility | With the article |
| Related research article | Author’s name: Deokyeol Jeong, Suji Ye, Heeyoung Park, and Soo Rin Kim |
The dataset contains the construction strategy and fermentation data for the engineered strain simultaneously fermenting representative three carbon sources (xylose, arabinose, galacturonic acid) in pectin-rich biomass. The fermentation data of the YE9 strain expressing the three pathways can be useful for process design utilizing pectin-rich biomass consisting mainly of galacturonic acid and arabinose. Based on the fermentation data of the YE9 strain, feasible options for strain engineering can be broadened for industrial bioprocesses. |