Optimisation d'une approche pour l'analyse de l'expression de gènes au niveau unicellulaire chez des sous-populations spécialisées de lymphocytes T CD4+ humaines

Chez les patients cancéreux, les cellules malignes sont souvent reconnues et détruites par les cellules T cytotoxiques du patient. C'est pourquoi, depuis plusieurs années, des recherches visent à produire des vaccins sensibilisant les cellules de l'immunité adaptative, afin de prévenir certains cancers. Bien que les vaccins ciblant les cellules T CD8+ (cytotoxiques) ont une efficacité in-vitro élevée, un vaccin pouvant cibler les cellules T CD8+ et CD4+ aurait une plus grande efficacité (1-3). En effet, les cellules T helper (CD4+) favorisent la production et la maintenance des cellules T CD8+ mémoires à longue durée de vie. Il existe un grand nombre de sous-types de cellules T CD4+ et leur action envers les cellules cancéreuses est différente. Par exemple, les lymphocytes Treg ont une activité pro-tumorale importante (4) et les lymphocytes Th1 ont une activité anti-tumorale (5). Cependant, le taux naturel des différents sous-types de cellules T CD4+ spécifiques aux antigènes tumoraux est variable. De plus, une certaine flexibilité des différents sous-types de cellules T CD4+ a été récemment démontrée (6). Celle-ci pourrait être ciblée par des protocoles de vaccination avec des antigènes tumoraux administrés conjointement à des adjuvants définis. Pour cela, il faut approfondir les connaissances sur le rôle des cellules T CD4+ spécifiques aux antigènes dans l'immunité anti-tumorale et connaître précisément la proportion des sous-types de cellules T CD4+ activées avant et après la vaccination. L'analyse des cellules T, par la cytométrie de flux, est très souvent limité par le besoin d'un nombre très élevé de cellules pour l'analyse de l'expression protéique. Or dans l'analyse des cellules T CD4+ spécifiques aux antigènes tumoraux cette technique n'est souvent pas applicable, car ces cellules sont présentes en très faible quantité dans le sang et dans les tissus tumoraux. C'est pourquoi, une approche basée sur l'analyse de la cellule T individuelle a été mise en place afin d'étudier l'expression du profil génétique des cellules T CD8+ et CD4+. (7,8) Méthode : Ce nouveau protocole (« single cell ») a été élaboré à partir d'une modification du protocole PCR-RT, qui permet la détection spécifique de l'ADN complémentaire (ADNc) après la transcription globale de l'ARN messager (ARNm) exprimé par une cellule T individuelle. Dans ce travail, nous optimisons cette nouvelle technique d'analyse pour les cellules T CD4+, en sélectionnant les meilleures amorces. Tout d'abord, des clones à profils fonctionnels connus sont générés par cytométrie de flux à partir de cellules T CD4+ d'un donneur sain. Pour cette étape d'optimisation des amorces, la spécificité des cellules T CD4+ n'est pas prise en considération. Il est, donc, possible d'étudier et de trier ces clones par cytométrie de flux. Ensuite, grâce au protocole « single cell », nous testons par PCR les amorces des différents facteurs spécifiques de chaque sous-type des T CD4+ sur des aliquotes issus d'une cellule provenant des clones générés. Nous sélectionnons les amorces dont la sensibilité, la spécificité ainsi que les valeurs prédictives positives et négatives des tests sont les meilleures. (9) Conclusion : Durant ce travail nous avons généré de l'ADNc de cellules T individuelles et sélectionné douze paires d'amorces pour l'identification des sous-types de cellules T CD4+ par la technique d'analyse PCR « single cell ». Les facteurs spécifiques aux cellules Th2 : IL-4, IL-5, IL-13, CRTh2, GATA3 ; les facteurs spécifiques aux cellules Th1 : TNFα, IL-2 ; les facteurs spécifiques aux cellules Treg : FOXP3, IL-2RA ; les facteurs spécifiques aux cellules Th17 : RORC, CCR6 et un facteur spécifique aux cellules naïves : CCR7. Ces amorces peuvent être utilisées dans le futur en combinaison avec des cellules antigènes-spécifiques triées par marquage des multimères pMHCII. Cette méthode permettra de comprendre le rôle ainsi que l'amplitude et la diversité fonctionnelle de la réponse de la cellule T CD4+ antigène-spécifique dans les cancers et dans d'autres maladies. Cela afin d'affiner les recherches en immunothérapie oncologique. (8)

Cost Optimisation of Mobile Advertising Client Data Transfer

Data traffic caused by mobile advertising client software when it is communicating with the network server can be a pain point for many application developers who are considering advertising-funded application distribution, since the cost of the data transfer might scare their users away from using the applications. For the thesis project, a simulation environment was built to mimic the real client-server solution for measuring the data transfer over varying types of connections with different usage scenarios. For optimising data transfer, a few general-purpose compressors and XML-specific compressors were tried for compressing the XML data, and a few protocol optimisations were implemented. For optimising the cost, cache usage was improved and pre-loading was enhanced to use free connections to load the data. The data traffic structure and the various optimisations were analysed, and it was found that the cache usage and pre-loading should be enhanced and that the protocol should be changed, with report aggregation and compression using WBXML or gzip.

Ultrafine grinding of FGD and phosphogypsum with an attrition bead mill and a jet mill : optimisation and modelling of grinding and mill comparison

Fine powders of minerals are used commonly in the paper and paint industry, and for ceramics. Research for utilizing of different waste materials in these applications is environmentally important. In this work, the ultrafine grinding of two waste gypsum materials, namely FGD (Flue Gas Desulphurisation) gypsum and phosphogypsum from a phosphoric acid plant, with the attrition bead mill and with the jet mill has been studied. The ' objective of this research was to test the suitability of the attrition bead mill and of the jet mill to produce gypsum powders with a particle size of a few microns. The grinding conditions were optimised by studying the influences of different operational grinding parameters on the grinding rate and on the energy consumption of the process in order to achieve a product fineness such as that required in the paper industry with as low energy consumption as possible. Based on experimental results, the most influential parameters in the attrition grinding were found to be the bead size, the stirrer type, and the stirring speed. The best conditions, based on the product fineness and specific energy consumption of grinding, for the attrition grinding process is to grind the material with small grinding beads and a high rotational speed of the stirrer. Also, by using some suitable grinding additive, a finer product is achieved with a lower energy consumption. In jet mill grinding the most influential parameters were the feed rate, the volumetric flow rate of the grinding air, and the height of the internal classification tube. The optimised condition for the jet is to grind with a small feed rate and with a large rate of volumetric flow rate of grinding air when the inside tube is low. The finer product with a larger rate of production was achieved with the attrition bead mill than with the jet mill, thus the attrition grinding is better for the ultrafine grinding of gypsum than the jet grinding. Finally the suitability of the population balance model for simulation of grinding processes has been studied with different S , B , and C functions. A new S function for the modelling of an attrition mill and a new C function for the modelling of a jet mill were developed. The suitability of the selected models with the developed grinding functions was tested by curve fitting the particle size distributions of the grinding products and then comparing the fitted size distributions to the measured particle sizes. According to the simulation results, the models are suitable for the estimation and simulation of the studied grinding processes.

Optimisation of the lipase-catalysed preparation of a nucleoside prodrug model using an experimental design methodology

The preparation of 2', 3'-di-O-hexanoyluridine (2) by a Candida antarctica B lipase-catalysed alcoholysis of 2', 3', 5'-tri-O-hexanoyluridine (1) was optimised using an experimental design. At 25 ºC better experimental conditions allowed an increase in the yield of 2 from 80% to 96%. In addition to the yield improvement, the volume reaction could be diminished in a factor of 5 and the reaction time significantly shortened.

Estudi sociomorfològica a Manresa : el segment velar en algunes formes del PI i el PS dels verbs anar, fer, veure i haver

Des d’una perspectiva sociomorfològica, aquest estudi analitza la correlació que hi ha entre les variables socials de l’edat, el gènere i la classe social i un dels trets morfofonològics més característics del parlar dels joves de Manresa: la presència del segment velar /g/ en la primera persona del singular del present d’indicatiu, i en les persones primera, segona i tercera del singular i en la tercera del plural del present de subjuntiu dels verbs irregulars anar, fer, veure i haver (ex. vaic i vaigui).

Use of experimental design in the optimisation of a solid phase preconcentration system for Cobalt determination by GFAAS

In this work is proposed a solid phase preconcentration system of Co2+ ions and its posterior determination by GFAAS in which fractional factorial design and response surface methodology (RSM) were used for optimization of the variables associated with preconcentration system performance. The method is based on cobalt extraction as a complex Co2+-PAN (1:2) in a mini-column of polyurethane foam (PUF) impregnated with 1-(2-pyridylazo)-naphthol (PAN) followed by elution with HCl solution and its determination by GFAAS. The chemical and flow variables studied were pH, buffer concentration, eluent concentration and preconcentration and elution flow rates. Results obtained from fractional factorial design 2(5-1) showed that only the variables pH, buffer concentration and interaction (pH X buffer concentration) based on analysis of variance (ANOVA) were statistically significant at 95% confidence level. Under optimised conditions, the method provided an enrichment factor of 11.6 fold with limit of detection and quantification of 38 and 130 ng L-1, respectively, and linear range varying from 0.13 to 10 µg L-1. The precision (n = 9) assessed by relative standard deviation (RSD) was respectively 5.18 and 2.87% for 0.3 and 3.0 µg L-1 cobalt concentrations.

Structural and operational optimisation : applications in energy systems

In this work mathematical programming models for structural and operational optimisation of energy systems are developed and applied to a selection of energy technology problems. The studied cases are taken from industrial processes and from large regional energy distribution systems. The models are based on Mixed Integer Linear Programming (MILP), Mixed Integer Non-Linear Programming (MINLP) and on a hybrid approach of a combination of Non-Linear Programming (NLP) and Genetic Algorithms (GA). The optimisation of the structure and operation of energy systems in urban regions is treated in the work. Firstly, distributed energy systems (DES) with different energy conversion units and annual variations of consumer heating and electricity demands are considered. Secondly, district cooling systems (DCS) with cooling demands for a large number of consumers are studied, with respect to a long term planning perspective regarding to given predictions of the consumer cooling demand development in a region. The work comprises also the development of applications for heat recovery systems (HRS), where paper machine dryer section HRS is taken as an illustrative example. The heat sources in these systems are moist air streams. Models are developed for different types of equipment price functions. The approach is based on partitioning of the overall temperature range of the system into a number of temperature intervals in order to take into account the strong nonlinearities due to condensation in the heat recovery exchangers. The influence of parameter variations on the solutions of heat recovery systems is analysed firstly by varying cost factors and secondly by varying process parameters. Point-optimal solutions by a fixed parameter approach are compared to robust solutions with given parameter variation ranges. In the work enhanced utilisation of excess heat in heat recovery systems with impingement drying, electricity generation with low grade excess heat and the use of absorption heat transformers to elevate a stream temperature above the excess heat temperature are also studied.

Production planning and optimization of a pulp mill: introduction of the optimisation based scheduling software for pulp industry

The objective of this project was to introduce a new software product to pulp industry, a new market for case company. An optimization based scheduling tool has been developed to allow pulp operations to better control their production processes and improve both production efficiency and stability. Both the work here and earlier research indicates that there is a potential for savings around 1-5%. All the supporting data is available today coming from distributed control systems, data historians and other existing sources. The pulp mill model together with the scheduler, allows what-if analyses of the impacts and timely feasibility of various external actions such as planned maintenance of any particular mill operation. The visibility gained from the model proves also to be a real benefit. The aim is to satisfy demand and gain extra profit, while achieving the required customer service level. Research effort has been put both in understanding the minimum features needed to satisfy the scheduling requirements in the industry and the overall existence of the market. A qualitative study was constructed to both identify competitive situation and the requirements vs. gaps on the market. It becomes clear that there is no such system on the marketplace today and also that there is room to improve target market overall process efficiency through such planning tool. This thesis also provides better overall understanding of the different processes in this particular industry for the case company.

Production of magnesium carbonates from serpentinites for CO2 mineral sequestration : optimisation towards industrial application

Global warming is one of the most alarming problems of this century. Initial scepticism concerning its validity is currently dwarfed by the intensification of extreme weather events whilst the gradual arising level of anthropogenic CO2 is pointed out as its main driver. Most of the greenhouse gas (GHG) emissions come from large point sources (heat and power production and industrial processes) and the continued use of fossil fuels requires quick and effective measures to meet the world’s energy demand whilst (at least) stabilizing CO2 atmospheric levels. The framework known as Carbon Capture and Storage (CCS) – or Carbon Capture Utilization and Storage (CCUS) – comprises a portfolio of technologies applicable to large‐scale GHG sources for preventing CO2 from entering the atmosphere. Amongst them, CO2 capture and mineralisation (CCM) presents the highest potential for CO2 sequestration as the predicted carbon storage capacity (as mineral carbonates) far exceeds the estimated levels of the worldwide identified fossil fuel reserves. The work presented in this thesis aims at taking a step forward to the deployment of an energy/cost effective process for simultaneous capture and storage of CO2 in the form of thermodynamically stable and environmentally friendly solid carbonates. R&D work on the process considered here began in 2007 at Åbo Akademi University in Finland. It involves the processing of magnesium silicate minerals with recyclable ammonium salts for extraction of magnesium at ambient pressure and 400‐440⁰C, followed by aqueous precipitation of magnesium in the form of hydroxide, Mg(OH)2, and finally Mg(OH)2 carbonation in a pressurised fluidized bed reactor at ~510⁰C and ~20 bar PCO2 to produce high purity MgCO3. Rock material taken from the Hitura nickel mine, Finland, and serpentinite collected from Bragança, Portugal, were tested for magnesium extraction with both ammonium sulphate and bisulphate (AS and ABS) for determination of optimal operation parameters, primarily: reaction time, reactor type and presence of moisture. Typical efficiencies range from 50 to 80% of magnesium extraction at 350‐450⁰C. In general ABS performs better than AS showing comparable efficiencies at lower temperature and reaction times. The best experimental results so far obtained include 80% magnesium extraction with ABS at 450⁰C in a laboratory scale rotary kiln and 70% Mg(OH)2 carbonation in the PFB at 500⁰C, 20 bar CO2 pressure for 15 minutes. The extraction reaction with ammonium salts is not at all selective towards magnesium. Other elements like iron, nickel, chromium, copper, etc., are also co‐extracted. Their separation, recovery and valorisation are addressed as well and found to be of great importance. The assessment of the exergetic performance of the process was carried out using Aspen Plus® software and pinch analysis technology. The choice of fluxing agent and its recovery method have a decisive sway in the performance of the process: AS is recovered by crystallisation and in general the whole process requires more exergy (2.48–5.09 GJ/tCO2sequestered) than ABS (2.48–4.47 GJ/tCO2sequestered) when ABS is recovered by thermal decomposition. However, the corrosive nature of molten ABS and operational problems inherent to thermal regeneration of ABS prohibit this route. Regeneration of ABS through addition of H2SO4 to AS (followed by crystallisation) results in an overall negative exergy balance (mainly at the expense of low grade heat) but will flood the system with sulphates. Although the ÅA route is still energy intensive, its performance is comparable to conventional CO2 capture methods using alkanolamine solvents. An energy‐neutral process is dependent on the availability and quality of nearby waste heat and economic viability might be achieved with: magnesium extraction and carbonation levels ≥ 90%, the processing of CO2‐containing flue gases (eliminating the expensive capture step) and production of marketable products.

Arrêt du conseil d'Etat qui nomme des commissaires pour procéder au jugement des oppositions formées au sceau des provisions des offices reçus en paiement des taxes des gens d'affaires ; à la liquidation des dettes privilégiées et à l'ordre des créanciers

[Acte. 1717-07-03. Paris]