A simple strategy for the purification of native recombinant full-length human RPL10 protein from inclusion bodies

Inclusion Bodies: Status Quo and Perspectives

Multiple E. coli cultivations, producing recombinant proteins, lead to the formation of inclusion bodies (IBs). IBs historically were considered as nondesired by-products, due to their time- and cost-intensive purification. Nowadays, many obstacles in IB processing can be overcome. As a consequence, several industrial processes with E. coli favor IB formation over soluble production options due to the high space time yields obtained. Within this chapter, we discuss the state-of-the art biopharmaceutical IB process, review its challenges, highlight the recent developments and perspectives, and also propose alternative solutions, compared to the state-of-the art processing.

A new approach for purification of the catalytic site of the angiotensin-conversion enzyme, N-domain, mediated by the ELP-Intein system

Angiotensin-converting enzyme I (ACE) is a key part of the renin-angiotensin system. Its main function is to regulate blood pressure and the balance of salts in the body. Somatic ACE has two domains, N-C-, each of which has a catalytic site that exhibits 60%sequence identity. The N-domain has a specific action in the hydrolysis of beta-amyloid bodies and angiotensin (1-7), which activates the MAS receptor and triggers anti-thrombotic and anti-inflammatory actions. Our goal was to obtain the catalytic site Ala³⁶¹ to Gly⁴⁶⁸ of the N domain region, csACE_N, without needing purification by chromatography. We employed a method that uses an Elastin-like Polypeptide (ELP) and Intein sequences linked to the peptide of interest. The more differential for obtaining the pure peptide was the cultivation temperatures in the synthesis of ELPcsACE_N at 37 °C, with a significant increase in expression. In the purification by ELP precipitation, we recorded the highest efficiency in the concentrations of 0.57 M and 0.8 M of ammonium sulfate buffer. Intein autocleavage study allows removal of the ELP sequence at acidic pH, with the buffers MES and Tris-HCl The present study defined the best conditions for obtaining pure csACE_N that the literature has not yet described for peptides. Obtaining pure csACE_N aims at future studies for therapeutic use in hypertension, Alzheimer's, and oncology.

Influence of the expression vector and its elements on recombinant human prolactin synthesis in Escherichia coli; co-directional orientation of replication and transcription is highly critical

The aim of the present work was to define a bacterial expression system that is particularly efficient for the synthesis of recombinant human prolactin (hPRL). In previous work, based on experiments that were basically carried out in parallel with the present ones, the synthesis of rec-hPRL by the p1813-hPRL vector in E. coli HB2151 was >500 mg/L, while it was much lower here (2.5-4-fold), in the RB791 and RRI strains. The highest positive influence on rec-hPRL synthesis was due to the transcription-replication co-orientation of hPRL cDNA and the ori/antibiotic resistance gene, responsible for up to a ~ 5-6-fold higher expression yield. In conclusion, this work confirmed that each bacterial strain of E. coli has a genetic background that can allow a different level of heterologous protein synthesis. The individual study of each element indicated that its action critically depends on the reading orientation in which it is located inside the vector: co-directional orientation of replication and transcription, in fact, greatly increased the level of rec-hPRL expression.

High production and optimization of the method for obtaining pure recombinant human prolactin

Prolactin is a pituitary hormone that is involved diverse physiological functions, such as lactation, reproduction, metabolism, osmoregulation, immunoregulation, and behavior. Its level of glycosylation is low in vivo, which favors its expression in bacterial systems. In the present work recombinant human prolactin (rec-hPRL) was expressed from the p1813-hPRL vector in Escherichia coli strain in inclusion bodies with 530.67 mg of rec-hPRL per liter of induced bacterial culture. The solubilization and renaturation of rec-hPRL followed by two methods described in the literature for this protein: one with detergent and basic pH, and other urea and dialyses was done by studying. The protocol with detergent/basic pH was not successful, whereas protocol with urea/dialyses was obtained pure protein and this was optimized. Rec-hPRL was obtained in a soluble, pure and active form, when the sample was 8-fold concentrated in the solubilization phase, allowing 33% recovery, 3-fold more that the original method. The pure protein was obtained with 38.37 i. u./mg activity, which is three times greater than that of the PRL standard from the WHO. In conclusion, this work obtained the highest production of rec-hPRL, and concentrating the sample eight times in the solubilization stage was decisive for obtaining a highly concentrated, active protein for future work.