Downstream purification often represents the most cost-intensive step in the manufacturing of recombinant proteins. Conventional purification processes are lengthy, technically complicated, product specific and time-consuming. To address this issue, herein we develop a one step purification system that due to the nature of the non-selective secretion system and the versatility of ion-exchange membrane chromatography can be widely applied to the production of many recombinant proteins. This was achieved through the integration of the intrinsically coupled upstream, midstream and downstream processes, a connection that is rarely exploited. A bioprocess for effective production and purification of penicillin G acylase (PAC) was developed. PAC was overexpressed in a genetically engineered Escherichia coli strain, secreted into the cultivation medium, harvested, and purified in a single step by anion-exchange chromatography. The cultivation medium developed had a sufficiently low conductivity to allow direct application of the extracellular fraction to the anion-exchange chromatography medium while providing all of the required nutrients for sustaining cell growth and PAC overexpression. It was contrived with the purposes of (i) providing sufficient osmolarity and buffering capacity, (ii) minimizing ionic species to facilitate the binding of extracellular proteins to anion-exchange medium, and (iii) enhancing PAC expression level and secretion efficiency. Employing this medium recipe the specific PAC activity reached a high level of 487 U/L/OD600, with more than 90% was localized in the extracellular medium. Both, the osmotic pressure and induction conditions were found to be critical for optimal culture performance. Furthermore, formation of inclusion bodies associated with PAC overexpression tended to arrest cell growth, leading to potential cell lysis. iv At harvest, the whole non-clarified culture broth was applied directly to a tangential flow filtration anion-exchange membrane chromatography system. One-step purification of recombinant PAC was achieved based on the dual nature of membrane chromatography (i.e. microfiltration-sized pores and anion-exchange chemistry). Due to their size, cells remained in the retentate while the extracellular medium penetrated the membrane. Most contaminate proteins were captured by the anion-exchange membrane, whereas the purified PAC was collected in the filtrate. The batch time for both cultivation and purification was less than 24 h and recombinant PAC with high purity (19 U/mg), process yield (74%), and productivity (41 mg/L) was obtained.

Downstream purification often represents the most cost-intensive step in the manufacturing of recombinant proteins. Conventional purification processes are lengthy, technically complicated, product specific and time-consuming. To address this issue, herein we develop a one step purification system that due to the nature of the non-selective secretion system and the versatility of ion-exchange membrane chromatography can be widely applied to the production of many recombinant proteins. This was achieved through the integration of the intrinsically coupled upstream, midstream and downstream processes, a connection that is rarely exploited. A bioprocess for effective production and purification of penicillin G acylase (PAC) was developed. PAC was overexpressed in a genetically engineered Escherichia coli strain, secreted into the cultivation medium, harvested, and purified in a single step by anion-exchange chromatography. The cultivation medium developed had a sufficiently low conductivity to allow direct application of the extracellular fraction to the anion-exchange chromatography medium while providing all of the required nutrients for sustaining cell growth and PAC overexpression. It was contrived with the purposes of (i) providing sufficient osmolarity and buffering capacity, (ii) minimizing ionic species to facilitate the binding of extracellular proteins to anion-exchange medium, and (iii) enhancing PAC expression level and secretion efficiency. Employing this medium recipe the specific PAC activity reached a high level of 487 U/L/OD600, with more than 90% was localized in the extracellular medium. Both, the osmotic pressure and induction conditions were found to be critical for optimal culture performance. Furthermore, formation of inclusion bodies associated with PAC overexpression tended to arrest cell growth, leading to potential cell lysis. iv At harvest, the whole non-clarified culture broth was applied directly to a tangential flow filtration anion-exchange membrane chromatography system. One-step purification of recombinant PAC was achieved based on the dual nature of membrane chromatography (i.e. microfiltration-sized pores and anion-exchange chemistry). Due to their size, cells remained in the retentate while the extracellular medium penetrated the membrane. Most contaminate proteins were captured by the anion-exchange membrane, whereas the purified PAC was collected in the filtrate. The batch time for both cultivation and purification was less than 24 h and recombinant PAC with high purity (19 U/mg), process yield (74%), and productivity (41 mg/L) was obtained.

No description available.

Flavonoid glycosyltransferases (GTs), enzymes integral to plant ecological responses and human pharmacology, necessitate rigorous structural elucidation to decipher their mechanistic function and substrate specificity, particularly given their role in the biotransformation of diverse pharmacological agents and natural products. This investigation delved into a comprehensive exploration of the flavonol 3-O GT from Citrus paradisi (Cp3GT), scrutinizing the impact of a c-terminal c-myc/6x histidine tag on its enzymatic activity and substrate specificity, and successfully achieving its purification to apparent homogeneity. This established a strong foundation for potential future crystallographic and other structure/function analyses. Through the strategic implementation of site-directed mutagenesis, a thrombin cleavage site was incorporated proximal to the tag, followed by cloning in Pichia pastoris, methanol-induced expression, and cobalt-affinity chromatography for initial purification stages. Notably, the recombinant tags did not exhibit a discernible influence on Cp3GT kinetics, substrate preference, pH optima, or metal interactions, maintaining its specificity towards flavonols at the 3-OH position and favoring glucosylation of quercetin and kaempferol. Subsequent purification steps, including MonoQ anion exchange and size-exclusion chromatography, yielded Cp3GT with ≥95% homogeneity. In silico molecular models of Cp3GT and its truncated variants, Cp3GTΔ80 and Cp3GTΔ10, were constructed using D-I-TASSER and COFACTOR to assess binding interactions with quercetin and kaempferol. Results indicated minimal interference of c-myc/6x-his tags with the native Cp3GT structure. This study not only lays a foundation for impending crystallographic studies, aiming to solidify the understanding of Cp3GT's stringent 3-O flavonol specificity, but also accentuates the potential of microbial expression platforms and plant metabolic engineering in producing beneficial compounds. To this end, a thorough review of four pivotal classes of plant secondary metabolites, flavonoids, alkaloids, betalains, and glucosinolates, was conducted. This will open avenues for further research and applications in biotechnological, medical, and agricultural domains.

A proteína A de superfície de pneumococo (PspA) é indispensável para a virulência da bactéria e foi escolhida para a elaboração de uma nova vacina conjugada contra S. pneumoniae. Para tanto foi desenvolvido um processo industrial de produção e purificação do fragmento recombinante da PspA clado 3 em E. coli. Cultivos descontínuos alimentados foram estabelecidos com glicose ou glicerol em reator de 5L, obtendo-se 62g/L de células secas e 3g/L de PspA3. As células foram lisadas por homogeneizador contínuo de alta pressão com eficiência de 96,7%. A centrifugação foi definida como etapa de clarificação. A sequência cromatográfica troca aniônica seguida de afinidade por Ni+2 rendeu os melhores resultados de pureza (81%) e recuperação (70%). A cromatografia de troca catiônica foi selecionada como terceira etapa do processo, definindo assim um processo de produção e purificação escalonável que possibilitou a obtenção de PspA3 com alto grau de pureza (90%). / The pneumococcal surface protein A (PspA) is indispensable for virulence of S. pneumoniae and it was the first choice as carrier for a new conjugated vaccine against S.pneumoniae. Hence, the purpose of this work was to develop an industrial production and purification process of a recombinant fragment PspA clade 3 (rfPspA3) in E. coli. Fed-batch cultivations in 5 L bioreactors with defined medium were carried out using glucose or glycerol as carbon sources. It was obtained 62 g/L of dry cell weight and 3 g/L of rfPspA3. Cells were disrupted with 96.7% of efficiency by high pressure continuous homogenizer. Centrifugation was defined for the clarification step. The sequence with Q- followed by IMAC-Sepharose yielded the best purity and recovery of rfPspA3 (81 and 70%, respectively). Cation exchange was chosen for the last chromatography. In conclusion, an industrial production and purification process was developed and rfPspA3 was obtained with high purity (90%).

La chromatographie mode mixte représente l’une des plus grandes évolutions de ces dernières années dans le domaine des bioséparations. Cette technique repose sur l'intervention de plusieurs types d'interactions au sein d'un seul et même support. Les résines de chromatographie mode mixte HEA, PPA et MEP HyperCel portent des groupements aliphatiques, aromatiques, thiophiliques ainsi que des groupements aminés protonables en différentes positions. Au moyen d’expériences de chromatographie, à l’aide de protéines standards aux propriétés spécifiques et de mélanges complexes, nous avons isolé ces différentes interactions. Nous avons mis en évidence l’intervention majeure d'au moins deux types d'interactions au sein de ces supports : interactions hydrophobes et électrostatiques. Nous avons pu observer le comportement des résines lors de variations de pH, de force ionique, de types de sels et de tampons ou lors de la présence d'autres composés organiques. Nous avons mis en évidence l'intervention combinée de ces types d'interactions lors des différentes phases de chromatographie. Le comportement des résines mode mixte a révélé des sélectivités particulières et dont le contrôle ciblé à l'aide de l'environnement a permis le développement de méthodes de purification efficaces et originales. Nous avons pu ainsi développer des applications telles que la purification de fragment d’anticorps (Fab’2) à partir de culture de cellules d’insectes, la capture de protéine de type MBP à partir d’extrait bactériens et la capture d’anticorps monoclonaux à partir de cellules de mammifères (CHO), et ainsi améliorer les conditions d’utilisation de la chromatographie en mode mixte. / Mixed mode chromatography is the most innovative technique for bioseparation. Mixed mode resins, as the term suggest, involves multiples types of interaction at the same time. HyperCel mixed mode resins, HEA, PPA and MEP, involve aliphatic, aromatic or thiophilic groups as well as protonable amine located in the spacer arm or as a head group. Using classical chromatographic experiments, standards proteins and complex mixtures, we highlighted the two major types of interactions involved: hydrophobic and electrostatic interactions. We specifically influenced these interactions by modifying the environment in terms of ionic strength, pH, salt types, and other compounds. The combination of these interactions during every phase of a chromatographic process has been demonstrated. Mixed mode resins thus offer unique selectivity that can be controlled by the environment. This allowed us to develop several applications from antibodies fragments capture from insect cells, to the purification of MBP-tagged proteins, through monoclonal antibody capture from CHO cells. We thus enhanced mixed mode chromatography.

A proteína A de superfície de pneumococo (PspA) é indispensável para a virulência da bactéria e foi escolhida para a elaboração de uma nova vacina conjugada contra S. pneumoniae. Para tanto foi desenvolvido um processo industrial de produção e purificação do fragmento recombinante da PspA clado 3 em E. coli. Cultivos descontínuos alimentados foram estabelecidos com glicose ou glicerol em reator de 5L, obtendo-se 62g/L de células secas e 3g/L de PspA3. As células foram lisadas por homogeneizador contínuo de alta pressão com eficiência de 96,7%. A centrifugação foi definida como etapa de clarificação. A sequência cromatográfica troca aniônica seguida de afinidade por Ni+2 rendeu os melhores resultados de pureza (81%) e recuperação (70%). A cromatografia de troca catiônica foi selecionada como terceira etapa do processo, definindo assim um processo de produção e purificação escalonável que possibilitou a obtenção de PspA3 com alto grau de pureza (90%). / The pneumococcal surface protein A (PspA) is indispensable for virulence of S. pneumoniae and it was the first choice as carrier for a new conjugated vaccine against S.pneumoniae. Hence, the purpose of this work was to develop an industrial production and purification process of a recombinant fragment PspA clade 3 (rfPspA3) in E. coli. Fed-batch cultivations in 5 L bioreactors with defined medium were carried out using glucose or glycerol as carbon sources. It was obtained 62 g/L of dry cell weight and 3 g/L of rfPspA3. Cells were disrupted with 96.7% of efficiency by high pressure continuous homogenizer. Centrifugation was defined for the clarification step. The sequence with Q- followed by IMAC-Sepharose yielded the best purity and recovery of rfPspA3 (81 and 70%, respectively). Cation exchange was chosen for the last chromatography. In conclusion, an industrial production and purification process was developed and rfPspA3 was obtained with high purity (90%).