Evidence map›Paper›PMID 35902409›Full record

ArticleApplied microbiology and biotechnology2022

Strategy for the design of a bioreactor for L-lysine immobilized fermentation using Corynebacterium glutamicum.

Gang Meng, Wei Zhao, Qingguo Liu, Chunguang Zhao, Yanan Zou, Nan Zhao, Dong Liu, Hanjie Ying, Wenjun Sun, Yong Chen

Erratum issuedAbstract read
PubMed Publisher
In one paragraph

Article in Applied microbiology and biotechnology, 2022. The graph could read no effect estimate from its abstract, so it casts no vote on the map. An erratum has been issued. Cited by 2 papers.

0numbers the graph read from it
0cells of the map it votes in
2citing papers in PubMed
0.3field-weighted citation impact, top 45% of its field
1 · What the graph read from it

What it found

Each row is one number read from the abstract, on the scale the paper reported it, with its interval. Left of the dashed line favours the treatment, right favours the comparator. Under each row is the sentence it came from. New to these charts? A ten-minute tutorial.

The abstract states no effect estimate the extractor could read, or names no intervention and outcome on the map, so this paper lights no cell and moves no belief. It is still indexed, cited and linked below.

2 · The registry

The trial behind it

Trials whose registry record cites this paper, or whose number appears in the abstract. A trial that started after this paper was published is citing it as background, not reporting it.

Neither the registry nor the abstract names a trial number. If this is a trial report, that itself is worth knowing.

3 · Its place in the literature

Who cites it

2 citing papers in PubMed, 5 citations in OpenAlex.

  1. Review
  2. Article
4 · The record

Corrections and comments

5 · Who and what money

Authors and funding

10 authors at 1 institution in 1 country.

Gang MengNingxia Yipin Biotechnology Co. Ltd, Yinchuan, China.
Wei ZhaoNanjing Hi-Tech Biological Technology Research Institute Co. Ltd, Nanjing, China.
Qingguo LiuNanjing Hi-Tech Biological Technology Research Institute Co. Ltd, Nanjing, China.
Chunguang ZhaoNingxia Yipin Biotechnology Co. Ltd, Yinchuan, China.
Yanan ZouNanjing Hi-Tech Biological Technology Research Institute Co. Ltd, Nanjing, China.
Nan ZhaoNanjing Hi-Tech Biological Technology Research Institute Co. Ltd, Nanjing, China.
Dong LiuCollege of Biotechnology and Pharmaceutical Engineering, Nanjing Tech University, Nanjing, China.
Hanjie YingCollege of Biotechnology and Pharmaceutical Engineering, Nanjing Tech University, Nanjing, China.
Wenjun SunCollege of Biotechnology and Pharmaceutical Engineering, Nanjing Tech University, Nanjing, China. sunwenjun@njtech.edu.cn.
Yong ChenCollege of Biotechnology and Pharmaceutical Engineering, Nanjing Tech University, Nanjing, China. chenyong1982@njtech.edu.cn.ORCID http://orcid.org/0000-0001-6913-6510
Nanjing Tech University · CN

Funding

No grant is acknowledged in the PubMed record.

6 · The paper itself

Abstract

Biofilm-immobilized fermentation is a novel strategy that has been utilized in L-lysine fermentation. In this study, we describe a strategy for designing bioreactors for immobilized fermentation. We have constructed steel structures in which the carriers can be sewn, forming several star-like structures with different angles, and changing the ventilation robot to the aeration tray. In a 10-L bioreactor, this structure with 12 angles assisted the immobilized system to remedy the gap between free-cell and immobilized fermentation in the conversion rate. In a 50-L bioreactor, this enlarged structure with 16 angles illustrated a 4.61% higher conversion rate than the free-cell fermentation (67.75%) and increased the production by 28.56%. This successful case is the first step towards to industrial production of biofilm-based immobilized fermentation.Key points• The designed steel structure is useful for L-lysine immobilized fermentation in a 10-L bioreactor.• The conversion rate of immobilized fermentation increased from 13.99 to 60.07% and is 1.03% higher than that of the free-cell fermentation.• The conversion rate of the redesigned 50-L bioreactor is higher than that of free-cell fermentation.

Indexed as

Corynebacterium glutamicumBioreactorsFermentationLysineSteelLysineSteelBioreactor designCorynebacterium glutamicumImmobilized fermentationIndustrial applicationL-lysine

Identifiers

PMID35902409
OpenAlexW4288425124

What OpenQuestion holds

Textmetadata
Read underepoch 390

Registered trials

None linked

Read under generation 80e0d062 · epoch 390. Bibliography from PubMed, PubMed Central and OpenAlex; grants from NIH RePORTER; trial links from ClinicalTrials.gov; estimates, votes and beliefs from the OpenQuestion graph.