Single chain antibody fragment display systems: a review / 生物工程学报

Single chain antibody fragment (scFv) is a small molecule composed of a variable region of heavy chain (VH) and a variable region of light chain (VL) of an antibody, and these two chains are connected by a flexible short peptide. scFv is the smallest functional fragment with complete antigen-binding activity, which contains both the antibody-recognizing site and the antigen-binding site. Compared with other antibodies, scFv has the advantages of small molecular weight, strong penetration, low immunogenicity, and easy expression. Currently, the most commonly used display systems for scFv mainly include the phage display system, ribosome display system, mRNA display system, yeast cell surface display system and mammalian cell display system. In recent years, with the development of scFv in the field of medicine, biology, and food safety, they have also attracted much attention in the sectors of biosynthesis and applied research. This review summarizes the advances of scFv display systems in recent years in order to facilitate scFv screening and application.

Cultivation of Pichia pastoris carrying the scFv anti LDL (-) antibody fragment. Effect of preculture carbon source

Abstract Antibodies and antibody fragments are nowadays among the most important biotechnological products, and Pichia pastoris is one of the most important vectors to produce them as well as other recombinant proteins. The conditions to effectively cultivate a P. pastoris strain previously genetically modified to produce the single-chain variable fragment anti low density lipoprotein (-) under the control of the alcohol oxidase promoter have been investigated in this study. In particular, it was evaluated if, and eventually how, the carbon source (glucose or glycerol) used in the preculture preceding cryopreservation in 20% glycerol influences both cell and antibody fragment productions either in flasks or in bioreactor. Although in flasks the volumetric productivity of the antibody fragment secreted by cells precultured, cryopreserved and reactivated in glycerol was 42.9% higher compared with cells precultured in glucose, the use of glycerol in bioreactor led to a remarkable shortening of the lag phase, thereby increasing it by no less than thrice compared to flasks. These results are quite promising in comparison with those reported in the literature for possible future industrial applications of this cultivation, taking into account that the overall process time was reduced by around 8 h.

Engenharia de anticorpos na busca por fragmentos funcionais para insumos de diagnóstico e aplicações terapêuticas / Antibody engineering in the search for functional fragments for diagnostic inputs and therapeutic applications

Anticorpos, agentes empregados no desenvolvimento de pesquisas biomédicas, no diagnóstico e na terapêutica, possuem elevada capacidade de interação aos mais variados ligantes, Estruturalmente são heterotetrameros constituídos por duas cadeias leves e duas cadeias pesadas com massa molecular de aproximadamente 150 kDa, Visando melhorar as características farmacocinéticas e minimizar possíveis reações adversas desencadeadas por imunoglobulinas de origem não humana, a engenharia molecular de anticorpos vem obtendo fragmentos de anticorpos como porções Fab, F(ab?)2, scFv e Fv, Em adição aos anticorpos convencionais, camelídeos produzem imunoglobulinas funcionais desprovidas de cadeia leve, onde o domínio variável da cadeia pesada, denominado VHH ou nanocorpo, é responsável pelo reconhecimento antigênico, Apresentando características adequadas ao desenvolvimento de fármacos com alta capacidade de neutralização, fragmentos VHHs vêm sendo propostos para uso em imunoterapia passiva ou em drug-delivery, No diagnóstico esses fragmentos podem ser aplicados na construção de biosensores ou na imagiologia, atuando na detecção de células cancerígenas, no monitoramento de tumores ou em alterações celulares...

Antibodies, agents employed for the development of biomedical research, diagnostic and therapeutic, have high ability to interact with different ligands. Structurally are heterotetramers constituted by two light and two heavy chains, with molecular weight of approximately 150 kDa. Aiming to improve the pharmacokinetic properties and minimize possible adverse reactions triggered by immunoglobulins of non-human origin, the molecular engineering of antibodies has been obtaining fragments of antibodies, such as Fab, F(ab?)2, Fv and scFv. In addition to the conventional antibodies, camelids produce functional immunoglobulins devoid of light chain, in which the variable domain, named VHH or nanocorpo, is able to recognize the antigen. With appropriate characteristics for the development of drugs with high neutralizing capacity, VHH fragments have been proposed for use in passive immunotherapy or drug-delivery. To the diagnosis, these fragments can be used to construct biosensors, in the imagiology , acting in the detection of cancer cells, tumor monitoring or cell changes...

Expression, production, and renaturation of a functional single-chain variable antibody fragment (scFv) against human ICAM-1

Intercellular adhesion molecule-1 (ICAM-1) is an important factor in the progression of inflammatory responses in vivo. To develop a new anti-inflammatory drug to block the biological activity of ICAM-1, we produced a monoclonal antibody (Ka=4.19×10−8 M) against human ICAM-1. The anti-ICAM-1 single-chain variable antibody fragment (scFv) was expressed at a high level as inclusion bodies in Escherichia coli. We refolded the scFv (Ka=2.35×10−7 M) by ion-exchange chromatography, dialysis, and dilution. The results showed that column chromatography refolding by high-performance Q Sepharose had remarkable advantages over conventional dilution and dialysis methods. Furthermore, the anti-ICAM-1 scFv yield of about 60 mg/L was higher with this method. The purity of the final product was greater than 90%, as shown by denaturing gel electrophoresis. Enzyme-linked immunosorbent assay, cell culture, and animal experiments were used to assess the immunological properties and biological activities of the renatured scFv.

Production of antibody fragment (Fab) throughout Escherichia coli fed-batch fermentation process: Changes in titre, location and form of product

Background: Recombinant proteins, including antibodies and antibody fragments, often contain disulfide bond bridges that are necessary for their folding, stability and function. Production of disulfide-bond-containing proteins in the periplasm of Escherichia coli has been very useful, due to unique characteristics of the periplasm, for obtaining fully active and correctly folded products and for alleviating downstream processing. Results: In this study, fed-batch cultivation of Escherichia coli (E. coli) for production of Fab D1.3, which is an anti-hen egg white lysozyme (HEWL) antibody fragment was carried out at 37ºC, and the bacterial cells were induced by adding 0.1 mM IPTG to the culture medium. Fermentor was sampled over the course of fermentation; the bacterial cells were centrifugally separated from the culture broth and subjected to osmotic shock (with excluding HEWL) and sonication procedures. The resulting fractions were analysed for Fab using a combination of ELISA, SDS-PAGE and Western blotting and changes in product titre, location, and form was assessed throughout growth. It was shown that osmotic shock released the Fab from the periplasm very efficiently and its efficacy was 20-45% more than sonication. This study demonstrates that, at high cell density cultivation in fermentor, target product can appear inside and outside the cells, depending on the time of induction. The maximum amount of Fab (47 mg/l) in the periplasm was reached at 14 hrs cultivation (4 hrs post induction), being suitable time for cell harvest, selective periplasmic extraction and downstream capture. The Fab increasingly leaked into the culture medium, and reached its maximum culture medium titre of ~78 mg/l after 6 hrs post induction. After 16 hrs cultivation (6 hrs post induction) the amount of Fab remained constant in different locations within and outside the cells. Western blot analysis of cell fractions showed that certain amount of the Fab was also produced in the cells as insoluble form. Conclusions: In this work we showed that the production of Fab in the periplasm during high cell density cultivation of E. coli in fermentor can be challenging as the product may appear in various locations within and outside the cells. To exploit the advantages of the periplasmic expression systems for purification in downstream processing, bacterial cells should be harvested when they maintain the majority of the target protein in their periplasmic space (i.e. 4 hrs post induction).