The development of effective methods to cryopreserve precious cell types has had tremendous impact on regenerative and transfusion medicine. Hematopoietic stem cell (HSC) transplants from cryopreserved umbilical cord blood (UCB) have been used for regenerative medicine therapies to treat conditions including hematological cancers and immodeficiencies. Red blood cell (RBC) cryopreservation in blood banks extends RBC storage time from 42 days (for hypothermic storage) to 10 years and can overcome shortages in blood supplies from the high demand of RBC transfusions. Currently, the most commonly utilized cryoprotectants are 10% dimethyl sulfoxide (DMSO) for UCB and 40% glycerol for RBCs. DMSO is significantly toxic both to cells and patients upon its infusion. Glycerol must be removed to <1% post-thaw using complicated, time consuming and expensive deglycerolization procedures prior to transfusion to prevent intravascular hemolysis. Thus, there is an urgent need for improvements in cryopreservation processes to reduce/eliminate the use of DMSO and glycerol. Ice recrystallization during cryopreservation is a significant contributor to cellular injury and reduced cell viability. Compounds capable of inhibiting this process are thus highly desirable as novel cryoprotectants to mitigate this damage. The first compounds discovered that were ice recrystallization inhibitors were the biological antifreezes (BAs), consisting of antifreeze proteins and glycoproteins (AFPs and AFGPs). As such, BAs have been explored as potential cryoprotectants, however this has been met with limited success. The thermal hysteresis (TH)activity and ice binding capabilities associated with these compounds can facilitate cellular damage, especially at the temperatures associated with cryopreservation. Consequently, compounds that possess “custom-tailored” antifreeze activity, meaning they exhibit the potent ice recrystallization inhibition (IRI) activity without the ability to bind to ice or exhibit TH activity,are highly desirable for potential use in cryopreservation. This thesis focuses on the rational design of potent ice recrystallization inhibitors and on elucidating important key structural motifs that are essential for potent IRI activity. While particular emphasis in on the development of small molecule IRIs, exploration into structural features that influence the IRI of natural and synthetic BAs and BA analogues is also described as these are some of the most potent inhibitors known to date. Furthermore, this thesis also investigates the use of small molecule IRIs for the cryopreservation of various different cell types to ascertain their potential as novel cryoprotectants to improve upon current cryopreservation protocols, in particular those used for the long-term storage of blood and blood products. Through structure-function studies the influence of (glyco)peptide length, glycosylation and solution structure for the IRI activity of synthetic AFGPs and their analogues is described. This thesis also explores the relationship between IRI, TH and cryopreservation ability of natural AFGPs, AFPs and mutants of AFPs. While these results further demonstrated that BAs are ineffective as cryoprotectants, it revealed the potential influence of ice crystal shape and growth progression on cell survival during cryopreservation. One of the most significant results of this thesis is the discovery of alkyl- and phenolicglycosides as the first small molecule ice recrystallization inhibitors. Prior to this discovery, all reported small molecules exhibited only a weak to moderate ability to inhibit ice recrystallization. To understand how these novel small molecules inhibit this process, structure-function studies were conducted on highly IRI active molecules. These results indicated that key structural features, including the configuration of carbons bearing hydroxyl groups and the configuration of the anomeric center bearing the aglycone, are crucial for potent activity. Furthermore, studies on the phenolic-glycosides determined that the presence of specific substituents and their position on the aryl ring could result in potent activity. Moreover, these studies underscored the sensitivity of IRI activity to structural modifications as simply altering a single atom or functional group on this substituent could be detrimental for activity. Finally, various IRI active small molecules were explored for their cryopreservation potential with different cell types including a human liver cell line (HepG2), HSCs obtained from human UCB, and RBCs obtained from human peripheral blood. A number of phenolic-glycosides were found to be effective cryo-additives for RBC freezing with significantly reduced glycerol concentrations (less than 15%). This is highly significant as it could drastically decrease the deglycerolization processing times that are required when RBCs are cryopreserved with 40% glycerol. Furthermore, it demonstrates the potential for IRI active small molecules as novel cryoprotectants that can improve upon current cryopreservation protocols that are limited in terms of the commonly used cryoprotectants, DMSO and glycerol.

Les glycoprotéines virales sont impliquées dans les deux principales étapes d’entrée des virus enveloppés dans leurs cellules hôtes : l’attachement des virus aux récepteurs cellulaires et la fusion des membranes virale et cellulaire. Je me suis d’abord attachée à l’étude structurale de la principale glycoprotéine, E2, de deux hépacivirus : la forme B du virus GB (GBV-B) et le virus de l’hépatite C (HCV). Mes tentatives de cristallisation de l’ectodomaine de la protéine E2 du GBV-B sont restées vaines, mais l’analyse des propriétés de ses fragments a suggéré un rôle de son extrémité C-terminale dans la liaison à son récepteur. En parallèle, j’ai co-cristallisé un peptide synthétique correspondant à la principale boucle de liaison de E2 à son récepteur, avec un fragment d’anticorps dirigé contre cette boucle. Etonnament, le peptide forme une hélice , en nette contradiction avec la conformation étendue adoptée dans un fragment du cœur de E2. Associé à des données biochimiques, cela suggère une flexibilité inattendue de cette région de l’ectodomaine d’E2. Dans un second temps, je me suis intéressée à la glycoprotéine F des baculovirus. J’ai résolu la structure du trimère d’un fragment tryptique de F dans sa conformation post-fusion. Cette structure a validé une prédiction selon laquelle la protéine F était une protéine de fusion de classe I homologue à celle des paramyxovirus. La protéine F des baculovirus est ainsi le premier exemple d’une protéine de fusion de classe I encodée par un virus à ADN. Mes résultats confortent donc l’hypothèse que toutes les protéines F ont un ancêtre commun et suggèrent un lien évolutif intéressant entre les virus à ADN, à ARN et leurs hôtes. / Viral glycoproteins are responsible for the two major steps in entry into host cells by enveloped viruses: 1) attachment to cellular receptor/s and 2) fusion of the viral and cellular membranes. My thesis concentrated first on the structural analysis of the major envelope glycoprotein E2 of two hepaciviruses: GB virus B (GBV-B) and hepatitis C virus (HCV). Crystallization of the GBV-B E2 ectodomain remained unsuccessful, but the characterization of truncated versions of E2 suggested an important role of its C-terminal moiety in receptor binding. In parallel, I co-crystallized a synthetic peptide mimicking HCV E2 with an antibody fragment directed against the major receptor-binding loop of E2 that is targeted by broadly neutralizing antibodies. The structure unexpectedly revealed an α-helical peptide conformation, which is in stark contrast to the extended conformation of this region observed in the structure of an E2 core fragment. Together with further biochemical evidence this suggests an unanticipated structural flexibility within this region in the context of the soluble E2 ectodomain. Secondly, I focused on the structural analysis of the baculovirus glycoprotein F. I determined the crystal structure of the post-fusion trimer of a trypsin-truncated F fragment. This structure confirmed previous predictions that baculovirus F protein adopts a class I fusion protein fold and is homologous to the paramyxovirus F protein. Baculovirus F is therefore the first class I fusion protein encoded by a DNA virus. My results support the hypothesis that F proteins may have a common ancestor and imply interesting evolutionary links between DNA and RNA viruses and their hosts.

Cardiovascular diseases (CVD) are the leading cause of morbidity and mortality in Europe. Over 4 million people die from CVDs annually and another 11 million people develops CVDs every year. These numbers show that there is a need for better diagnostic, prognostic and predictive biomarkers and, more importantly, a need for new and more efficient drugs. Integral membrane proteins (IMPs) are ideal candidates for new drug targets. However, a study of IMPs represents a major challenge in current proteomics. This challenge is associated with the low abundance of IMPs, their low solubility in aqueous solvents and the absence of trypsin cleavage sites in their transmembrane segments. To overcome these issues, methods that selectively target either N-glycosylated extra-membrane segments (CSC, SPEG, N-glyco-FASP) or transmembrane segments (hpTC) were developed. In this thesis we employed a combination of two N-glyco-capture methods (SPEG and N-glyco-FASP) performed on two different samples (membrane-enriched fraction and total tissue lysate) with analysis of membrane-embedded IMP segments by hpTC and with standard non-targeted "detergent+trypsin" approach to analyze rat myocardial membrane proteome. We also performed an evaluation of employed methods for preparation of membrane fraction by western blot...

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Diss. (sammanfattning) Umeå : Umeå universitet, 2009. / Härtill 4 uppsatser. Även tryckt utgåva.

Diss. (sammanfattning) Stockholm : Karolinska institutet, 2009. / Härtill 4 uppsatser.

Du fait de leur présence à la surface de la particule virale, les glycoprotéines d’enveloppe E1 et E2 du virus HCV jouent un rôle essentiel dans sa morphogenèse ainsi que lors de son entrée dans la cellule hôte. Jusqu’à récemment, les travaux de recherche sur les glycoprotéines d’enveloppe du virus HCV se sont essentiellement focalisés sur E2 car elle est la protéine d’attachement du virus. De plus, elle est la cible majeure des anticorps neutralisants et il a été longtemps postulé qu’elle était la protéine de fusion du virus. Cependant, les récentes publications de la structure de E2 ne mettent pas en évidence la présence d’un peptide de fusion et sa structure ne correspond pas aux critères attendus pour une protéine de fusion, suggérant que la glycoprotéine E1 seule ou en association avec E2 pourrait être responsable de l’étape de fusion. La structure de la région N-terminale de E1 (acides aminés 192 à 270) a récemment été résolue et a mis en évidence la présence d’une épingle à cheveux formée par 2 feuillets beta (β1 et β2) suivie par un segment de 16 acides aminés qui forme une hélice alpha (α1) flanquant 3 feuillets beta antiparallèles (β3, β4 et β5). En plus de la caractérisation de ces structures secondaires de E1, une région qui se situe au milieu de la protéine (approximativement entre les résidus 274 et 292) a été proposée avoir un rôle actif au cours du processus de fusion et elle pourrait correspondre à un peptide de fusion.Nous nous sommes basés sur ces travaux récents pour investiguer le rôle fonctionnel de la glycoprotéine E1 par une approche de mutagenèse dirigée des résidus conservés dans la région N-terminale et dans la région du potentiel peptide de fusion, dans le contexte d’un clone infectieux du HCV. Comme attendu, nos résultats indiquent que ces mutations introduites dans E1 n’ont aucun effet sur la réplication virale. Cependant, vingt-et-un parmi les vingt-huit mutants produits conduisent à une atténuation ou une perte de l’infectiosité virale. D’une manière très intéressante, deux mutants atténués, le T213A et le I262A, se sont montrés moins dépendants au co-récepteur claudine-1. D’autre part, nous avons montré que ces mutants utilisent un autre récepteur de la famille des claudines (claudine-6) pour l’entrée virale, indiquant ainsi un changement de dépendance à son co-récepteur claudine-1. A l’opposé, deux autres mutants, le L286A et le E303A, se sont révélés avoir une plus grande dépendance au co-récepteur claudin-1 pour l’entrée dans les cellules d’hépatome. Au cours de ce travail, nous avons également identifié une mutation intéressante à proximité du potentiel peptide de fusion. Cette mutation, G311A, conduit à la sécrétion de particules virales entières mais non infectieuses, suggérant un défaut d’entrée cellulaire pour ce virus. De façon très surprenante, nous avons également identifié une mutation (D263A) qui conduit à la sécrétion de particules virales dépourvues d’ARN génomique. Une caractérisation plus poussée de ce mutant a de plus révélé une modification dans la co-localisation subcellulaire entre l'ARN viral et la glycoprotéine E1, mettant en évidence pour la première fois un dialogue croisé entre E1 et l'ARN génomique du HCV lors de la morphogenèse du virus.En conclusion, nos observations permettent d’identifier précisément les régions spécifiques de la protéine E1 qui jouent un rôle dans l’assemblage et l’entrée du virus dans la cellule, mettant en évidence le rôle majeur de la glycoprotéine E1 au niveau des différentes étapes du cycle infectieux du HCV. / Being part of the viral particle, HCV envelope glycoproteins E1 and E2 play an essential role in virion morphogenesis as well as in HCV entry into liver cells. These glycoproteins form a non-covalent heterodimer, and until recently, research on HCV envelope glycoproteins has been mainly focused on E2. Indeed, this glycoprotein is the receptor-binding protein, it is also the major target of neutralizing antibodies and it was postulated to be the fusion protein. However, the recent publications of the structure of E2 do not show the presence of a fusion peptide and its structure does not fit with what one would expect for a fusion protein, suggesting that E1 alone or in association with E2 might be responsible for the fusion step. Concerning E1, only the crystal structure of the two-fifth N-terminal region, comprising amino acids 192 to 270, has been reported. This partial structure reveals a complex network of covalently linked, intertwined homodimers. The overall fold of the N-terminal E1 monomer consists of a beta-hairpin (β1 and β2) followed by a segment composed of a 16 amino-acid long alpha-helix (α1) flanking a three-strand antiparallel beta-sheet (β3, β4 and β5). In addition to the characterization of secondary structures within E1, a region located in the middle of the polypeptide (approximately between aa 274 and 292) has been suggested to play an active role during the fusion process and might potentially act as a fusion peptide. We took advantage of these recently published data to further investigate the functional role of HCV glycoprotein E1 by using a site-directed mutagenesis approach targeting conserved amino acids in the N-terminal region as well as in the region postulated to contain the fusion peptide in the context of an infectious clone. As expected, our results indicate that these mutations have no effect on virus replication. However, twenty-one out of twenty-eight mutations led to attenuation or inactivation of infectivity. Interestingly, two attenuated mutants, T213A and I262A, were less dependent on tight junction protein claudin-1, a co-receptor for HCV. Instead, these mutant viruses relied on another claudin (claudin-6) for cellular entry, indicating a shift in receptor dependence. In contrast, two other mutants, L286 and E303, were more dependent on claudin-1 for cellular entry into hepatoma cells cells. We also identified an interesting mutation downstream of the putative fusion peptide, G311A, which leads to the release of non-infectious particles having a defect in cellular entry. Finally, an unexpected phenotype was also observed for D263A mutant, which was no longer infectious but led to the secretion of viral particles devoid of genomic RNA. Further characterization of the D263A mutant revealed a change in subcellular co-localization between HCV RNA and E1, highlighting for the first time a crosstalk between HCV glycoprotein E1 and the genomic RNA during HCV morphogenesis.In conclusion, our observations allowed for the identification of specific regions in the E1 glycoprotein that play a role in virion assembly and entry, highlighting the major role played by this protein at different steps of the HCV infectious cycle.

Thesis (MScEng)--Stellenbosch University, 2012. / ENGLISH ABSTRACT: Recombinant glycoproteins are important biopharmaceuticals, providing solutions for numerous previously untreatable illnesses, in everything from cancer to infertility. Most recombinant biopharmaceuticals are produced in mammalian cells due to their ability to provide the correct post-translational processing for use in humans. The post-translation processing influences many of the protein’s properties including pharmacokinetics, bioactivity, secretion, half-life, solubility, recognition and antigenicity. The aim of this thesis is to further study the upstream production of a glycosylated recombinant protein produced by Chinese hamster ovary (CHO) cells on production scale within the confines of an existing process. The process in question uses adherent CHO cells to produce a glycosylated recombinant hormone. As with most recombinant protein production processes, this process has two sections to the upstream production: a seed train to grow enough cells to inoculate production, and a production section, which focuses on the production of a recombinant protein. The seed train is predominantly conducted in roller bottles, while the production section takes place in perfusion bioreactors, where the cells are attached to microcarriers, with spin-filters for cell retention. The whole process uses medium with serum. There are two process challenges regarding an existing recombinant-protein production process: 1. The gradual increase, over the past several campaigns, of the final population doubling level of the cells (which must remain within certain specified limits) at the end of the seed train. 2. The low glycosylation levels of the product seen in certain campaigns, which meant that a certain number of final product batches were below the specified acceptable glycosylation limits. Following a literature survey several controlled process variables were chosen for investigation and hypotheses made on their effect on the seed train or glycosylation. To investigate their effect on the PDL and cell growth in the seed train: - Medium volume: decreasing the medium volume will yield a lower PDL due to slower cell growth caused by lower glucose availability. - Seeding density: if cells obtain confluence by the time they are harvested, decreasing the seeding density will yield a higher PDL. - Cultivation temperature: decreasing the temperature ought to decrease the growth rate. - Medium feed temperature: there will be no significant difference to the cell culture when pre-heated or cold medium is used. Aeration: using vent caps will increase the oxygen content of the medium in the roller bottles and the cell growth, yielding a higher PDL. To investigate their effect on glycosylation during production: - pH: better glycosylation will be seen at pH 6.9, than at pH 6.7. - Perfusion rate: a higher perfusion rate will lead to better glycosylation due to increased glucose and glutamine concentrations. In the seed train, the only factor that significantly influenced the final PDL was the seeding density. Cell growth was inhibited once cells reached confluence, so lowering the seeding density lead to a higher PDL. It is recommended to use a high seeding density to ensure a lower PDL. Historic data indicated that the seeding density was not the cause of the apparent increase of the final PDL, as all previous campaigns had been seeded with a high seeding density. What then became apparent was that the final PDL remained relatively constant during a campaign and that the increase in final PDL occurred between campaigns. It appears that the apparent increase in the final PDL is due to differences in cell counting between operators as each new campaign was managed by different operators. It is recommended that a mechanical cell counter be used to verify cells counts and to maintain a standard between campaigns. In the bioreactors, varying the pH proved to have no significant effect on the glycosylation levels. However, both the initial perfusion rate and the specific perfusion rate proved to be important from both historical data and the data generated during these experiments. Lower levels of the initial perfusion rate lead to better glycosylation and it is recommended that an initial perfusion rate of 1.0 volumes/day be used. The relationship between the specific perfusion rate and the glycosylation appears to be non-linear and requires further study, for now it is recommended that the specific perfusion rate be kept below 0.3 volumes/day/109 cells. Probable reasons for the unsatisfactory glycosylation seen in certain runs could also be proposed from these two factors: • RP33-133 : Very high specific perfusion rate • RP32-135 : High initial perfusion rate and very high specific perfusion rate • RP32-138 : High initial perfusion rate • RP33-139 : High initial perfusion rate Further research is recommended into the effect of the specific perfusion rate as well as the specific glucose consumption rate and the specific glutamine concentration on the glycosylation. / AFRIKAANSE OPSOMMING: Rekombinante glikoproteïene is baie belangrike biofarmaseutiese produkte wat oplossings bied vir talle voorheen ongeneeslike siektes in alles van kanker tot onvrugbaarheid. Meeste rekombinante farmaseutiese produkte word gemaak deur diere-selle as gevolg van hulle bevoegtheid om die korrekte na-translasie stappe te volg sodat die produkte in mense gebruik kan word. Die na-translasie stappe beïnvloed baie van die proteïene se karaktertreke insluitende die farmakokinetika, bioaktiwiteit, uitskeiding, half-leeftyd, oplosbaarheid, herkenbaarheid and antigeniciteit. Die doel van hierdie tesis is om die stroomop produksie van ‘n rekombinante glikoproteïene vervaardig deur Chinese hamster ovariale (CHO) selle verder te bestudeer binne die grense van ‘n bestaande proses op grootskaalse vlak. Die huidige proses gebruik CHO selle om ‘n rekombinante glikohormoon te produseer. Soos meeste prosesse wat rekombinante proteïene produseer bestaan die stroomop gedeelte van die proses uit twee dele: ‘n saad trein wat genoeg selle maak vir produksie en ‘n produksie gedeelte wat fokus op die vervaardiging van die glikoproteïen. Die saad trein bestaan hoofsaaklik uit roller bottels terwyl produksie plaasvind in perfusie bioreaktors waar die selle op “microcarriers” groei, met spin-filters om die selle binne die bioreaktors te hou; die hele proses gebruik medium met serum. Daar is twee probleme in die stroomop gedeelte van die bestaande proses: 1. Die geleidelike toename oor die afgelope paar jaar van die finale verdubbelingsvlak van die selle aan die einde van die saad trein 2. Die lae glukosilering van die eindproduk wat veroorsaak dat sekere lotnommers buite spesifikasie is Na ‘n literatuur studie, was seker beheerde proses parameters gekies om verder te bestudeer en hipotesisse gemaak oor hulle effek op die saad trein of die vlak van glukosilering. Die volgende faktore is bestudeer vir hulle effek op die finale verdubbelingsvlak van die selle in die saad trein: - Medium volume: ‘n laer medium volume sal lei tot a laer verdubbelingsvlak van die selle as gevolg van stadige groei - Konsentrasie van selle vir inokulasie: as die selle konfluent is teen die tyd wat hulle versamel word sal ‘n laer konsentrasie selle lei tot ’n hoër verdubellingsvlak. - Temperatuur: laer temperatuur behoort te lei tot ‘n stadiger groei koers van die selle - Medium voer-temperatuur: die voer-temperatuur van die medium sal geen beduidende verskil maak - Belugting: die gebruik van “vent-caps” sal die suurstof inhoud van die roller bottels verhoog Die volgende faktore is bestudeer vir hulle effek op die glukosilering tydens produksie: - pH: beter glukosilering word verwag by by pH 6.9 dan by pH 6.7 - Perfusie koers: ‘n hoër perfusie koers sal lei tot beter glukosilering as gevolg van hoër glukose en glutamien konsentrasies Die konsentrasie van die selle wat gebruik word vir inokulasie blyk die enigste faktor te wees wat die finale verdubbelingsvlak van die selle en die groei van die selle in die saad trein beïnvloed het. Die groei van die selle was beprek wanneer die selle konfluent geraak het en dus het ‘n laër sel konsentrasie by inokulasie gelei tot ‘n hoër sel verdubbelingsvlak. Dit word aanbeveel dat ‘n hoë sel konsentrasie by inokulasie gebruik word. Die geleidelike toename van die finale verdubbelingsvlak van die selle in die saad trein is waarskynlik as gevolg van die variasie in sel tellings tussen verskillende operateurs eerder as as gevolg van die beheerde proses parameters. Dit word aanbeveel dat ‘n meganiese sel-teller gebruik word om die verskil in sel tellings tussen operateurs te kontroleer en om ‘n standaard te handhaaf tussen produksie lotte. In die bioreaktors, het die pH geen beduidende invloed gehad op die glukosilering maar uit historiese data en die huidige data van hierdie eksperimente blyk albei die begin perfusie koers en die spesifieke perfusie koers ‘n belangrike invloed te hê op die glukosilering. Laër vlakke van die begin perfusie koers lei tot beter glikosilsie en dit word aanbeveel dat elke produksielot ‘n begin perfusie koers het van 1.0 volume/dag. Die verhouding tussen die glukosilering en die spesifieke perfusie koers blyk om nie-liniêr te wees nie. Nog navorsing hieroor word aanbeveel, maar vir nou word dit aanbeveel dat die spesifieke perfusie koers onder 0.3 volumes/dag/109 selle gehou word. Hierde twee faktore blyk die oorsaak te wees vir die lae glukosilering wat in sekere produksielopies gevind was: • RP33-133 : baie hoë spesifieke perfusie koers • RP32-135 : hoë begin perfusie koers en baie hoe spesifieke perfusie koers • RP32-138 : hoë begin perfusie koers • RP33-139 : hoë begin perfusie koers Dit word aanbeveel dat verdere navorsing gedoen word op die effek van die spesifieke perfusie koers asook die spesifieke koers van glukose verbruik en die spesifieke glutamien konsentrasie op die glukosilering van die produk.

published_or_final_version / Microbiology / Doctoral / Doctor of Philosophy