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Biomedical subjects

Pei Xu

Publications and source records attributed to Pei Xu.

7 recordsLinked to original sources

Development of a multi-copy integration platform in Kluyveromyces marxianus enabled by a computational method for genome-wide identification of multi-copy integration loci.

Multi-copy integration is a core strategy for redirecting metabolic flux toward target compounds. However, its application has been hampered by the absence of methods for systematically identifying native multi-copy genomic loci. To overcome this, we developed a computational procedure for genome-wide identification of such loci. Theoretically, this method is potentially applicable to any genome-sequenced species as it only requires the genomic assembly of the target species as input. Applying the procedure to Kluyveromyces marxianus, we identified four groups of loci (KmCS1-4). Combining these loci-KmCS1-4 and the traditional 26S rDNA-with 14 markers with graded selection strengths, we established a versatile multi-copy integration toolkit comprising 70 plasmids. Each plasmid exhibits a unique integration pattern, collectively forming an integration profile. This profile serves as a manual, enabling users to select appropriate tools tailored to the expression requirements of rate-limiting enzymes in their pathways. Applying representative plasmids exhibiting low-, medium-, and high-copy integration patterns to lycopene biosynthesis modules resulted in lycopene titers of 3.5, 6.8 and 40.5 mg/L, corresponding to 2, 6 and 9 genomic copies, respectively, demonstrating a positive correlation between lycopene titers, genomic copy numbers and integration patterns, which highlights the versatility of the toolkit and its supporting manual. Our study not only provides a broadly applicable methodology for genome-wide identification of multi-copy loci, but also an efficient integration platform for K. marxianus.

Kluyveromyces marxianus↗

cTrans: generating polypeptide databases from cDNA sequences.

cTrans is a comprehensive utility used to generate polypeptide databases from cDNA sequences. The goal is achieved through integrating four main functions, including retrieving sequences of species of interest from the downloaded packages from dbEST of GenBank, format conversion, checking and deleting vector and adaptor contamination, and translating the cDNA sequences in all six frames and selecting specific translations for database construction in a user-defined length threshold. In addition, this utility is also applicable to cDNA sequences produced by users themselves.

Base Sequence↗

High-concentration food wastewater treatment by an anaerobic membrane bioreactor.

The viability of treating high-concentration food wastewater by an anaerobic membrane bioreactor (AMBR) was studied using polyethersulfone (PES) ultrafiltration membranes PES200, PES300, PES500 and PES700 with norminal molecular weight cutoff (MWCO) ranging from 20,000 to 70,000 Da. Hydraulic and solid retention time significantly affected the treatment performance of the AMBR kept at 60 h and 50 days in the study. The four membranes exhibited a similar efficiency in removal of suspended solids, color, chemical oxygen demand (COD) and bacteria. When the volumetric loading rate was below 4.5 kg/m3d, COD removal rate was in the range of 81-94% and the gas yield stabilized at 0.136 m3/kg COD. The effect of membrane properties including MWCO, hydrophobicity and surface morphology on membrane fouling and cleaning was evaluated. The PES200 membranes with the smallest MWCO and smoothest surface exhibited a serious initial flux decline, whereas the PES700 membranes with the largest MWCO and roughest surface were observed related to the highest flux decline and the lowest recoverable flux rate during long-term operation. Membrane autopsy revealed that the significant flux decline was caused by the formation of a thick biofouling layer onto the membrane surfaces.

Anaerobiosis↗

Factors affecting the rejection of organic solutes during NF/RO treatment--a literature review.

The incomplete rejection of certain pesticides, disinfection by-products, endocrine disrupting compounds, and pharmaceutically active compounds has been reported during full- and pilot-scale high-pressure membrane applications. Since the removal of these compounds in water and wastewater treatment applications is of great importance where a high product water quality is desired, an understanding of the factors affecting the permeation of solutes in high-pressure membrane systems is needed. In this paper, findings of a comprehensive literature review are reported, targeting membrane rejection mechanisms and factors affecting rejection. The following key solute parameters were identified to primarily affect solute rejection: molecular weight (MW), molecular size (length and width), acid disassociation constant (pKa), hydrophobicity/hydrophilicity (log Kow), and diffusion coefficient (Dp). Key membrane properties affecting rejection that were identified include molecular weight cut-off, pore size, surface charge (measured as zeta potential), hydrophobicity/hydrophilicity (measured as contact angle), and surface morphology (measured as roughness). In addition, feed water composition, such as pH, ionic strength, hardness, and the presence of organic matter, was also identified as having an influence on solute rejection. From the knowledge gained during the literature review, a rejection diagram was proposed, which qualitatively allows prediction of solute rejection if certain solute and membrane properties are known.

Hydrogen-Ion Concentration↗

Wastewater disinfection by ozone: main parameters for process design.

Wastewater disinfection by ozone was investigated at pilot scale on different wastewater effluents. Variations in operating conditions showed that a very low hydraulic retention time (2 min) was sufficient for efficient fecal coliform inactivation, provided a sufficient ozone dose was transferred to the effluent. Therefore, the transferred ozone dose appeared to be the critical parameter for the design of wastewater disinfection. As a consequence, the "Ct" approach commonly applied in drinking water treatment should not be used for wastewater ozonation. Design parameters of ozonation were proposed for two types of regulations, and for effluents of different qualities. It was demonstrated that only with an efficient filtration step one can meet stringent standards such as the California Title 22 criteria. In all cases, viruses were totally inactivated; consequently, viruses do not constitute a limiting factor in wastewater disinfection by ozone. The standard drinking water model failed to match the experimental data obtained on real wastewater effluents. A modified approach was successfully developed, based on the simultaneous consumption of ozone by the microorganisms and the organic matrix.

Bioreactors↗

Rejection of emerging organic micropollutants in nanofiltration-reverse osmosis membrane applications.

The rejection of emerging trace organics by a variety of commercial reverse osmosis (RO), nanofiltration (NF), and ultra-low-pressure RO (ULPRO) membranes was investigated using TFC-HR, NF-90, NF-200, TFC-SR2, and XLE spiral membrane elements (Koch Membrane Systems, Wilmington, Massachusetts) to simulate operational conditions for drinking-water treatment and wastewater reclamation. In general, the presence of effluent organic matter (EfOM) improved the rejection of ionic organics by tight NF and RO membranes, as compared to a type-II water matrix (adjusted by ionic strength and hardness), likely as a result of a decreased negatively charged membrane surface. Rejection of ionic pharmaceutical residues and pesticides exceeded 95% by NF-90, XLE, and TFC-HR membranes and was above 89% for the NF-200 membrane. Hydrophobic nonionic compounds, such as bromoform and chloroform, exhibited a high initial rejection, as a result of both hydrophobic-hydrophobic solute-membrane interactions and steric exclusion, but rejection decreased significantly after 10 hours of operation because of partitioning of solutes through the membranes. This resulted in a partial removal of disinfection byproducts by the RO membrane TFC-HR. In a type-II water matrix, the effect of increasing feed water recoveries on rejection of hydrophilic ionic and nonionic compounds was compound-dependent and not consistent for different membranes. The presence of EfOM, however, could neutralize the effect of hydrodynamic operating condition on rejection performance. The ULPRO and tight NF membranes were operated at lower feed pressure, as compared to the TFC-HR, and provided a product water quality similar to a conventional RO membrane, regarding trace organics of interest.

Disinfection↗