Article(id=1304366241460809884, tenantId=1146029695717560320, journalId=1192105938417971205, issueId=1304366133864321404, articleNumber=null, orderNo=null, doi=10.13343/j.cnki.wsxb.20260354, pmid=null, cstr=null, oa=null, hot=null, price=null, onlineType=0, articleFormat=0, articleType=null, articleTypeStr=research-article, receivedDate=1777392000000, receivedDateStr=2026-04-29, revisedDate=null, revisedDateStr=null, acceptedDate=1780588800000, acceptedDateStr=2026-06-05, onlineDate=1788914745916, onlineDateStr=2026-09-09, pubDate=1788451200000, pubDateStr=2026-09-04, doiRegisterDate=null, doiRegisterDateStr=null, onlineIssueDate=1788914745916, onlineIssueDateStr=2026-09-09, onlineJustAcceptDate=null, onlineJustAcceptDateStr=null, onlineFirstDate=null, onlineFirstDateStr=null, sourceXml=null, magXml=null, createTime=1788914745916, creator=13701087609, updateTime=1788914745916, updator=13701087609, issue=Issue{id=1304366133864321404, tenantId=1146029695717560320, journalId=1192105938417971205, year='2026', volume='66', issue='9', pageStart='4291', pageEnd='4651', issueExtLink='null', onlineDate='null', pubDate='1788451200000', pubDateStr='2026-09-04', beforeIssueId=null, nextIssueId=null, price=null, status=1, issueComplete=1, articleOrder=1, issueType=1, specialIssue=0, createTime=1788914720263, creator='13701087609', updateTime=1788914779113, updator='13701087609', preIssue=null, nextIssue=null, articleTotal=null, ext={EN=IssueExt(id=1304366380803974113, tenantId=1146029695717560320, journalId=1192105938417971205, issueId=1304366133864321404, language=EN, specialIssueTitle=, coverIllustrator=null, specialIssueEditor=, specialIssueAbout=), CN=IssueExt(id=1304366380803974114, tenantId=1146029695717560320, journalId=1192105938417971205, issueId=1304366133864321404, language=CN, specialIssueTitle=, coverIllustrator=null, specialIssueEditor=, specialIssueAbout=)}, issueFiles=null, downloadFileDto=null}, startPage=4545, endPage=4566, ext={EN=ArticleExt(id=1304366241926377629, articleId=1304366241460809884, tenantId=1146029695717560320, journalId=1192105938417971205, language=EN, title=From C1/C2 feedstocks to single-cell proteins: biomanufacturing routes and challenges, columnId=1192149543727808575, journalTitle=Acta Microbiologica Sinica, columnName=Review, runingTitle=null, highlight=null, articleAbstract=
As efficient and sustainable proteins, single-cell proteins (SCPs) demonstrate significant potential in alleviating the constraints of traditional agricultural resources and reducing the carbon footprint of food manufacturing. Low-carbon C1/C2 feedstocks, such as carbon dioxide, methanol, and acetate, offer distinct advantages, including broad availability, low costs, and minimal carbon footprints. However, the assimilation of these feedstocks and the accumulation of proteins are still limited by key bottlenecks such as poor host cell adaptability, imbalanced metabolic flux distribution, and inefficient energy supply. In recent years, remarkable progress has been achieved in the discovery, evaluation, and rational engineering of host strains for the efficient bioconversion of C1/C2 feedstocks. The application of synthetic biology, metabolic engineering, and laboratory adaptive evolution has enabled the continuous improvements of the strain tolerance to C1/C2 feedstocks, assimilation efficiency, and intracellular protein accumulation capacity. On the basis of these advancements, various SCP production processes utilizing C1/C2 feedstocks are gradually advancing toward pilot-scale and industrial applications. This review systematically summarizes the strategies for constructing chassis cells that efficiently utilize C1/C2 feedstocks, key metabolic engineering technologies driving efficient SCP production, and the current technological and industrial status of SCP production from different C1/C2 feedstocks. Furthermore, it discusses challenges related to energy efficiency, nutritional quality, safety, and downstream scale-up, aiming to provide a theoretical foundation and technical reference for the sustainable development and industrial application of SCPs produced from C1/C2 feedstocks.
, authors=Jing QIU
1, 2, 3, Qinhong WANG
1, 3, Zongjie DAI
1, 2, 3, *, Yanhe MA
1, 3, authorsList=Jing QIU, Qinhong WANG, Zongjie DAI, Yanhe MA, authorCompany=null, correspAuthors=Zongjie DAI, authorNote=null, correspAuthorsNote=
, copyrightStatement=null, copyrightOwner=null, extLink=null, articleAbsUrl=null, sourceXml=null, magXml=null, pdfUrl=null, pdf=null, pdfFileSize=null, pdfExtLink=null, richHtmlUrl=null, mobilePdfUrl=null, reviewReport=null, pdfFirstPage=null, abstractGraph=null, abstractGraphContent=null, abstractVideo=null, citation=null, cebUrl=null, magXmlContent=null, mapNumber=null, fund=null), CN=ArticleExt(id=1304366245432815778, articleId=1304366241460809884, tenantId=1146029695717560320, journalId=1192105938417971205, language=CN, title=从
C1/C2底物到单细胞蛋白:生物制造路径与挑战, columnId=1192149543882997826, journalTitle=微生物学报, columnName=综述, runingTitle=null, highlight=null, articleAbstract=
单细胞蛋白(single-cell protein, SCP)作为一种高效、可持续的蛋白质来源,在缓解传统农业资源约束和降低食品制造碳足迹方面展现出重要潜力。二氧化碳、甲醇、乙酸等低碳C1/C2底物具有来源广泛、成本低廉、碳足迹小等优势,但其同化效率与蛋白高效积累仍受限于底盘细胞适配性不足、代谢通量分配失衡以及能量供给效率低下等关键瓶颈。近年来,围绕C1/C2底物的高效生物转化,研究者已在微生物底盘的挖掘、评价与理性改造方面取得显著进展,并通过代谢工程、合成生物学及实验室适应进化等手段,持续提升菌株对C1/C2底物的耐受性、同化效率及胞内蛋白质积累能力。在此基础上,多种基于C1/C2底物的SCP生产工艺正逐步向中试及规模化应用推进。本文系统综述了C1/C2底物高效利用底盘细胞的构建策略、代谢工程驱动SCP高效生产的关键技术,以及不同C1/C2底物生产SCP的技术发展与产业化现状,并进一步探讨了能量效率、营养品质、安全性及规模化放大等方面面临的挑战,以期为C1/C2底物生产SCP的可持续发展与工业应用提供理论依据与技术参考。
, authors=邱靖
1, 2, 3, 王钦宏
1, 3, 戴宗杰
1, 2, 3, *, 马延和
1, 3, authorsList=邱靖, 王钦宏, 戴宗杰, 马延和, authorCompany=null, correspAuthors=戴宗杰, authorNote=
作者贡献声明
邱靖:提出概念,撰写文章,编辑、修改;王钦宏、戴宗杰:获取基金,提出概念,审阅与修改;马延和:总体思路指导。
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1.State Key Laboratory of Engineering Biology for Low-Carbon Manufacturing, Tianjin Institute of Industrial Biotechnology, Chinese Academy of Sciences, Tianjin, China
2.Sino-Danish College, University of Chinese Academy of Sciences, Beijing, China
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1.中国科学院天津工业生物技术研究所,低碳合成工程生物学全国重点实验室,天津
2.中国科学院大学 中丹学院,北京
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1.State Key Laboratory of Engineering Biology for Low-Carbon Manufacturing, Tianjin Institute of Industrial Biotechnology, Chinese Academy of Sciences, Tianjin, China
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1.中国科学院天津工业生物技术研究所,低碳合成工程生物学全国重点实验室,天津
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1, 2, 3, *, address=
1.State Key Laboratory of Engineering Biology for Low-Carbon Manufacturing, Tianjin Institute of Industrial Biotechnology, Chinese Academy of Sciences, Tianjin, China
2.Sino-Danish College, University of Chinese Academy of Sciences, Beijing, China
3.National Center of Technology Innovation for Synthetic Biology, Tianjin, China, bio=null, bioImg=null, bioContent=null, aboutCorrespAuthor=null), CN=AuthorExt(id=1304492620877689626, tenantId=1146029695717560320, journalId=1192105938417971205, articleId=1304366241460809884, authorId=1304492620516979477, language=CN, stringName=戴宗杰, firstName=null, middleName=null, lastName=null, prefix=null, suffix=null, authorComment=null, nameInitials=null, affiliation=null, department=null, xref=
1, 2, 3, *, address=
1.中国科学院天津工业生物技术研究所,低碳合成工程生物学全国重点实验室,天津
2.中国科学院大学 中丹学院,北京
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1, 3, address=
1.State Key Laboratory of Engineering Biology for Low-Carbon Manufacturing, Tianjin Institute of Industrial Biotechnology, Chinese Academy of Sciences, Tianjin, China
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1.中国科学院天津工业生物技术研究所,低碳合成工程生物学全国重点实验室,天津
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Zhu Y. The invention relates to a preparation device for producing unicellular protein based on acetic acid as a raw material: CN217838917U[P]. 2022-11-18., articleTitle=null, refAbstract=null)], funds=[Fund(id=1304492623922754355, tenantId=1146029695717560320, journalId=1192105938417971205, articleId=1304366241460809884, awardId=25ZXZSSS00480, language=EN, fundingSource=the Science and Technology Program of Tianjin(25ZXZSSS00480), fundOrder=null, country=null), Fund(id=1304492623994057524, tenantId=1146029695717560320, journalId=1192105938417971205, articleId=1304366241460809884, awardId=25ZXZSSS00480, language=CN, fundingSource=天津市科技计划(25ZXZSSS00480), fundOrder=null, country=null)], companyList=[AuthorCompany(id=1304492617597743870, tenantId=1146029695717560320, journalId=1192105938417971205, articleId=1304366241460809884, xref=1., ext=[AuthorCompanyExt(id=1304492617618715391, tenantId=1146029695717560320, journalId=1192105938417971205, articleId=1304366241460809884, companyId=1304492617597743870, language=EN, country=null, province=null, city=null, postcode=null, companyName=null, departmentName=null, remark=
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Overview of single-cell protein production from C1/C2 feedstocks. The production of SCP from C1/C2 feedstocks is primarily achieved through the assimilation of carbon dioxide, carbon monoxide, methanol, formate, acetate, or ethanol by bacteria, yeasts, fungi, and microalgae. Metabolic engineering strategies have successfully integrated heterologous C1/C2 assimilation pathways into conventional microbial cell factories. To date, synthetic pathways with enhanced carbon assimilation efficiency and reduced energetic requirements have also been developed. The performance of these C1/C2 feedstocks SCP producers can be further augmented through evolutionary and gene-editing strategies, as well as coupling with electrochemical technologies. However, the industrialization of SCP still faces critical challenges regarding scale-up fermentation optimization, downstream processing development, regulatory approval systems, and market penetration. SCP: Single-cell protein; RuMP: Ribulose monophosphate pathway; rGly: Reductive glycine pathway; CBB: Calvin-Benson-Bassham cycle; ACS: Acetyl-CoA synthase pathway; ACK-PTA: Acetate kinase-phosphotransacetylase pathway; MES: Microbial electrosynthesis system; ALE: Adaptive lab evolution; HTS: High-throughput screening., figureFileSmall=+de3mdhtdZr4r5GjhIFXHw==, figureFileBig=LxkNySOKUX++cEszf5onMA==, tableContent=null), ArticleFig(id=1304492622966453036, tenantId=1146029695717560320, journalId=1192105938417971205, articleId=1304366241460809884, language=CN, label=图1, caption=
C1/C2底物单细胞蛋白生产总览, figureFileSmall=+de3mdhtdZr4r5GjhIFXHw==, figureFileBig=LxkNySOKUX++cEszf5onMA==, tableContent=null), ArticleFig(id=1304492623062922029, tenantId=1146029695717560320, journalId=1192105938417971205, articleId=1304366241460809884, language=EN, label=Figure 2, caption=
Metabolic engineering strategies for optimizing single-cell protein biosynthesis. In terms of carbon metabolism, redirecting carbon flux toward protein synthesis can be achieved by disrupting non-essential carbon metabolic pathways. For nitrogen metabolism, reinforcing the expression levels of key pathway enzymes and optimizing inter-amino acid conversions provide sufficient substrates for protein biosynthesis. To enhance the protein quality, promising strategies include strengthening branched-chain amino acid biosynthetic pathways or de novo designed proteins with high BCAAs content. Furthermore, global regulatory approaches, such as blocking the HOG signaling pathway, increasing cell volume, and enhancing translation efficiency can be implemented to achieve efficient protein accumulation within the strains. SCP: Single-cell protein; AA: Amino acids; HOG pathway: High-osmolarity glycerol pathway; BCAAs: Branched-chain amino acids., figureFileSmall=z5CV1clnlewbFlM+UrQ9UA==, figureFileBig=oqWjf1/HUtthuALC8IPg4g==, tableContent=null), ArticleFig(id=1304492623125836590, tenantId=1146029695717560320, journalId=1192105938417971205, articleId=1304366241460809884, language=CN, label=图2, caption=
优化单细胞蛋白合成的代谢工程策略, figureFileSmall=z5CV1clnlewbFlM+UrQ9UA==, figureFileBig=oqWjf1/HUtthuALC8IPg4g==, tableContent=null), ArticleFig(id=1304492623209722671, tenantId=1146029695717560320, journalId=1192105938417971205, articleId=1304366241460809884, language=EN, label=Table 1, caption=
Evolution strategies for improving C1/C2 feedstock tolerance of strains
, figureFileSmall=null, figureFileBig=null, tableContent=
| C1/C2 feedstocks | Strains | Evolution strategies | Results and achievements | References |
|---|
| Carbon dioxide | Synechococcus elongatus PCC7942 | Gradient ALE from 5.0% to 20.0% CO2 | Identified potential key genes: pbsA, pyk, dnaA, MutS | [23] |
| C. autoethanogenum | Chemostat ALE at 23.0% CO2 in a bioreactor | Identified potential key genes: perR, gerKA, prfB, thrB, argR | [24] |
| Desertifilum sp. | Gradient ALE from 5.0% to 15.0% CO2 | Increased chlorophyll a, carotenoid, and enhanced antioxidant systems contribute to CO2 tolerance | [25] |
| Nannochloropsis oceanica | Stationary and gradient ALE from 6.0% to 99.0% CO2 | Mutations tend to be directed toward light-harvesting proteins | [26] |
| Cupriavidus necator | Atmospheric and room temperature plasma (ARTP) mutagenesis combined with strain screening under atmosphere of H2:O2:CO2 at 7:1:1 | Identified key mutations LysS (C437T) and key gene gapdh | [27] |
| Formic acid/formate | Methylorubrum extorquens AM1 | Gradient ALE from 30.0 to 90.0 mmol/L sodium formate | Identified key genes: META1_0287, META1_3027, META1_3028, META1_3029, META1_1261, META1_1418, META1_2965 | [28] |
| Y. lipolytica | Gradient ALE from 4.0% to 6.6% formate | Identified key gene Ftl1 | [29] |
| E. coli | Stationary ALE at 60.0 mmol/L formate | Identified key mutation lacO (G8A) | [30] |
| E. coli | Stationary ALE at 90.0 mmol/L formate | Inhibition of acetate metabolism is beneficial for improving formate metabolism | [31] |
| Vibrio natriegens | Gradient ALE from 20.0 to 140.0 g/L formate | Identified potential key mutations: fumA (A44E) and sdhC insertion | [32] |
| Chlamydomonas reinhardtii | Gradient and stationary ALE from 50.0 to 60.0 mmol/L formate | The alleviation of formate inhibition is associated with increased carbonic anhydrase activity | [33] |
| E. coli | Gradient and stationary ALE from 70.0 to 120.0 mmol/L formate | Identified potential key genes: ptnAB and thrA | [34] |
| S. cerevisiae | CRISPRi library screening combined with the “Scan-o-Matic” platform | Identified key genes: RPL33A, RPL30, RPL5, RPS3, TIF5, TIF34, TIF35, RVB1, RVB2, SNF2, SNF6, SWI3, HSF1, YPI1, SEC23, SEC24, RPT5, RPN8, RPT3, RPT4, RPN7, RPN12 | [35] |
| Methanol | P. pastoris | Stationary ALE at 5.0% and 7.0% methanol | Identified key genes: PSR1 and BFA1 | [36] |
| E. coli | NTG mutagenesis combined with gradient ALE from 1.0 to 3.0 mol/L methanol | Identified key genes: rpsL and rpsQ | [20] |
| Rhodotorula toruloides | Stationary ALE at 3.0% and 3.5% methanol | Carbon flux toward the biosynthesis of glycerolipid-related metabolites was regulated | [37] |
| Methylobacterium extorquens | Gradient ALE from 0.5% to 2.5% methanol | Identified key mutations: metY (F36L, S383L) and a premature stop codon in kefB | [38] |
| S. cerevisiae | Cyclic ALE between 0.0 and 2.0% methanol | Identified key mutation in YGR067C and key genes AHD2 and ACS1 | [39] |
| P. pastoris | Gradient ALE from 6.0% to 10.0% methanol | Identified key gene PET2 | [40] |
| Corynebacterium glutamicum | Stationary ALE at 15 g/L methanol | Identified key mutations: cgl0653 (G1256A) and cgl0833 (C1439T) | [41] |
| Acetic acid/acetate | Halomonas bluephagenesis | Gradient ALE from 20.0 to 120.0 g/L acetate | Enhanced flux of the TCA cycle and poly-(3-hydroxybutyrate) biosynthesis alleviates acetate toxicity | [42] |
| S. cerevisiae | Gradient ALE from 3.0 to 12.0 g/L acetic acid | Identified key genes: HSF1, SKN7, BAS1, WAR1, ASC1, GPA2, RAS2, and IRA2 | [43-44] |
| Chlorella vulgaris | Gradient ALE from 30.0 to 45.0 mmol/L sodium acetate | Acetate stress simultaneously improves carotenoid accumulation and wastewater treatment efficiency | [45] |
| Papiliotrema laurentii | Gradient ALE from 0.7 to 1.5 g/L sodium acetate | Identified key enzyme: glucan 1,3-β- glucosidase | [46] |
| Saccharomyces pastorinous | Stationary ALE at 0.6% acetic acid | High concentrations of acetate trigger ACS expression | [47] |
| Y. lipolytica | CRISPRi library screening | Identified key gene: YALI1_F12842g | [48] |
| S. cerevisiae | CRISPRi/CRISPRa library screening | Analyzed mechanisms of Pdr1 and Yap1 in acetate tolerance | [49] |
| Ethanol | S. cerevisiae | Cyclic ALE with increasing ethanol shock | The evolved strain significantly accelerated wine fermentation | [50-51] |
| S. cerevisiae | Cyclic ALE with increasing ethanol shock | Identified key mutations: cyr1 (A1474T) and usv1Δ | [52] |
), ArticleFig(id=1304492623381689136, tenantId=1146029695717560320, journalId=1192105938417971205, articleId=1304366241460809884, language=CN, label=表1, caption=
提升菌株C1/C2底物耐受性的进化策略
, figureFileSmall=null, figureFileBig=null, tableContent=
| C1/C2 feedstocks | Strains | Evolution strategies | Results and achievements | References |
|---|
| Carbon dioxide | Synechococcus elongatus PCC7942 | Gradient ALE from 5.0% to 20.0% CO2 | Identified potential key genes: pbsA, pyk, dnaA, MutS | [23] |
| C. autoethanogenum | Chemostat ALE at 23.0% CO2 in a bioreactor | Identified potential key genes: perR, gerKA, prfB, thrB, argR | [24] |
| Desertifilum sp. | Gradient ALE from 5.0% to 15.0% CO2 | Increased chlorophyll a, carotenoid, and enhanced antioxidant systems contribute to CO2 tolerance | [25] |
| Nannochloropsis oceanica | Stationary and gradient ALE from 6.0% to 99.0% CO2 | Mutations tend to be directed toward light-harvesting proteins | [26] |
| Cupriavidus necator | Atmospheric and room temperature plasma (ARTP) mutagenesis combined with strain screening under atmosphere of H2:O2:CO2 at 7:1:1 | Identified key mutations LysS (C437T) and key gene gapdh | [27] |
| Formic acid/formate | Methylorubrum extorquens AM1 | Gradient ALE from 30.0 to 90.0 mmol/L sodium formate | Identified key genes: META1_0287, META1_3027, META1_3028, META1_3029, META1_1261, META1_1418, META1_2965 | [28] |
| Y. lipolytica | Gradient ALE from 4.0% to 6.6% formate | Identified key gene Ftl1 | [29] |
| E. coli | Stationary ALE at 60.0 mmol/L formate | Identified key mutation lacO (G8A) | [30] |
| E. coli | Stationary ALE at 90.0 mmol/L formate | Inhibition of acetate metabolism is beneficial for improving formate metabolism | [31] |
| Vibrio natriegens | Gradient ALE from 20.0 to 140.0 g/L formate | Identified potential key mutations: fumA (A44E) and sdhC insertion | [32] |
| Chlamydomonas reinhardtii | Gradient and stationary ALE from 50.0 to 60.0 mmol/L formate | The alleviation of formate inhibition is associated with increased carbonic anhydrase activity | [33] |
| E. coli | Gradient and stationary ALE from 70.0 to 120.0 mmol/L formate | Identified potential key genes: ptnAB and thrA | [34] |
| S. cerevisiae | CRISPRi library screening combined with the “Scan-o-Matic” platform | Identified key genes: RPL33A, RPL30, RPL5, RPS3, TIF5, TIF34, TIF35, RVB1, RVB2, SNF2, SNF6, SWI3, HSF1, YPI1, SEC23, SEC24, RPT5, RPN8, RPT3, RPT4, RPN7, RPN12 | [35] |
| Methanol | P. pastoris | Stationary ALE at 5.0% and 7.0% methanol | Identified key genes: PSR1 and BFA1 | [36] |
| E. coli | NTG mutagenesis combined with gradient ALE from 1.0 to 3.0 mol/L methanol | Identified key genes: rpsL and rpsQ | [20] |
| Rhodotorula toruloides | Stationary ALE at 3.0% and 3.5% methanol | Carbon flux toward the biosynthesis of glycerolipid-related metabolites was regulated | [37] |
| Methylobacterium extorquens | Gradient ALE from 0.5% to 2.5% methanol | Identified key mutations: metY (F36L, S383L) and a premature stop codon in kefB | [38] |
| S. cerevisiae | Cyclic ALE between 0.0 and 2.0% methanol | Identified key mutation in YGR067C and key genes AHD2 and ACS1 | [39] |
| P. pastoris | Gradient ALE from 6.0% to 10.0% methanol | Identified key gene PET2 | [40] |
| Corynebacterium glutamicum | Stationary ALE at 15 g/L methanol | Identified key mutations: cgl0653 (G1256A) and cgl0833 (C1439T) | [41] |
| Acetic acid/acetate | Halomonas bluephagenesis | Gradient ALE from 20.0 to 120.0 g/L acetate | Enhanced flux of the TCA cycle and poly-(3-hydroxybutyrate) biosynthesis alleviates acetate toxicity | [42] |
| S. cerevisiae | Gradient ALE from 3.0 to 12.0 g/L acetic acid | Identified key genes: HSF1, SKN7, BAS1, WAR1, ASC1, GPA2, RAS2, and IRA2 | [43-44] |
| Chlorella vulgaris | Gradient ALE from 30.0 to 45.0 mmol/L sodium acetate | Acetate stress simultaneously improves carotenoid accumulation and wastewater treatment efficiency | [45] |
| Papiliotrema laurentii | Gradient ALE from 0.7 to 1.5 g/L sodium acetate | Identified key enzyme: glucan 1,3-β- glucosidase | [46] |
| Saccharomyces pastorinous | Stationary ALE at 0.6% acetic acid | High concentrations of acetate trigger ACS expression | [47] |
| Y. lipolytica | CRISPRi library screening | Identified key gene: YALI1_F12842g | [48] |
| S. cerevisiae | CRISPRi/CRISPRa library screening | Analyzed mechanisms of Pdr1 and Yap1 in acetate tolerance | [49] |
| Ethanol | S. cerevisiae | Cyclic ALE with increasing ethanol shock | The evolved strain significantly accelerated wine fermentation | [50-51] |
| S. cerevisiae | Cyclic ALE with increasing ethanol shock | Identified key mutations: cyr1 (A1474T) and usv1Δ | [52] |
), ArticleFig(id=1304492623461380913, tenantId=1146029695717560320, journalId=1192105938417971205, articleId=1304366241460809884, language=EN, label=Table 2, caption=
Comparation of representative industrialization projects for SCP from C1/C2 feedstocks
, figureFileSmall=null, figureFileBig=null, tableContent=
| Enterprise | Chassis | Carbon source | Productivity | Product application | Current status | Advantages |
|---|
| Shougang Lanzatech | C. autoethanogenum | CO | Current: 25 000 t/a | Feed protein | Obtained the certificate of new feed approval Achieve industrialized replication and rollout in Hebei, Ningxia, and Guizhou | Low cost: utilizing industrial waste gas as feeding |
| GTL Biotech | Y. lipolytica | CO2 | Current: 10 000 t/a Factory under construction: 300 000 t/a | Feed protein | Obtained the certificate of new feed approval Completed the industrial-scale trial production | Electrocatalytic carbon fixation coupled with high-density fermentation |
| Aerbio | HOB | CO2 | Current: 2.4 t/a Factory under construction: 100 000 t/a | Feed protein & pet food | Completed EU feed ingredient registration Conduct applied research on feed formulation in collaboration with BioMar The pilot production line has commenced continuous commercial operation | One-step anaerobic fermentation Zero carbon footprint |
| Solar Foods | HOB | CO2 | Current: 160 t/a Factory under construction: 6 400 t/a | Functional foods & everyday foods | The product has obtained novel food approval in Singapore and Generally Recognized as Safe (GRAS) certification in the United States | Good food processing properties |
| JingFuture Biotechnology | P. pastoris | Methanol | Current: 10 000 t/a Factory under construction: 200 000 t/a | Feed protein | The demonstration line is operating stably | High-density fermentation |
), ArticleFig(id=1304492623566238514, tenantId=1146029695717560320, journalId=1192105938417971205, articleId=1304366241460809884, language=CN, label=表2, caption=
代表性C1/C2底物SCP产业化项目对比
, figureFileSmall=null, figureFileBig=null, tableContent=
| Enterprise | Chassis | Carbon source | Productivity | Product application | Current status | Advantages |
|---|
| Shougang Lanzatech | C. autoethanogenum | CO | Current: 25 000 t/a | Feed protein | Obtained the certificate of new feed approval Achieve industrialized replication and rollout in Hebei, Ningxia, and Guizhou | Low cost: utilizing industrial waste gas as feeding |
| GTL Biotech | Y. lipolytica | CO2 | Current: 10 000 t/a Factory under construction: 300 000 t/a | Feed protein | Obtained the certificate of new feed approval Completed the industrial-scale trial production | Electrocatalytic carbon fixation coupled with high-density fermentation |
| Aerbio | HOB | CO2 | Current: 2.4 t/a Factory under construction: 100 000 t/a | Feed protein & pet food | Completed EU feed ingredient registration Conduct applied research on feed formulation in collaboration with BioMar The pilot production line has commenced continuous commercial operation | One-step anaerobic fermentation Zero carbon footprint |
| Solar Foods | HOB | CO2 | Current: 160 t/a Factory under construction: 6 400 t/a | Functional foods & everyday foods | The product has obtained novel food approval in Singapore and Generally Recognized as Safe (GRAS) certification in the United States | Good food processing properties |
| JingFuture Biotechnology | P. pastoris | Methanol | Current: 10 000 t/a Factory under construction: 200 000 t/a | Feed protein | The demonstration line is operating stably | High-density fermentation |
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