Thesis--University of California, Berkeley, 1959. / "Biology and Medicine" -t.p. Includes bibliographical references (p. 50-55).

Thesis (Ph. D.)--University of Washington, 2003. / Vita. Includes bibliographical references (leaves 96-104).

The primary goal of this project is to develop an experimental setup for testing membrane materials. The membranes tested are all porous, hydrophilic and non- selective. The secondary goal is that the module finds use as an educational tool for learning about diffusion on a university level. The final setup consisted of two modified 250 ml polyethylene bottles with a wide neck joined together with a flange pinning the test object in between. In the experiments one side is loaded with a sodium chloride solution, while the other is loaded with pure deionized water. The conductivity change is then monitored in the chamber loaded with deionized water using a conductivity probe. Two test subjects are tested, an alpha Cellulose filter and a polycarbonate membrane. The mass transfer coefficient are determined to be 8.99*10-6 ± 3.90*10-6 [cm/min] and 3.62*10-5 ± 1.49*10-6 [cm/min] respectively. The large inconsistencies in the alpha cellulose filters results in large standard deviations, whereas the polycarbonate is very consistent and therefore have very small error bars. Meaning that the largest error in this design originates from inconsistencies between samples of the test subject. The setup is suitable as an educational tool due to short run times of one hour, the generated data only requires simple linear regression to extract mass transfer coefficients from the slope. The experiment can be varied further by adjusting temperature and stirring. / Det primära målet med det här projektet är att utveckla en experimentell uppställning för att testa membran. Alla testade membran är porösa, hydrofila och icke-selektiva. Det sekundära målet är att uppställningen kan användas som ett pedagogiskt verktyg för kurser i masstransport. Den slutliga uppställningen består av två modifierade 250 ml polyeten flaskor med vid hals, ihopsatta med en fläns som håller testobjektet på plats emellan flaskorna. I experimenten fylls en av kamrarna med saltlösning och den andra med avjoniserat vatten, konduktiviteten mäts i kammaren som laddas med avjoniserat vatten. Två objekt testades, ett alfacellulosa filter och ett polykarbonat membran. Massöverförings koefficienter bestämdes till 8.99*10-6 ± 3.90*10-6 [cm/min] för alfacellulosa filtret och 3.62*10-5 ± 1.49*10-6 [cm/min] för polykarbonat membranet. Det finns stora variationer i alfacellulosa materialet vilket leder till stora standardavvikelse i körningarna på alfacellulosa filtret, medan polykarbonat membranen var identiska och därmed har väldigt små felstaplar. Därmed kunde det fastslås att stora avvikelser nästan bara beror på variationer i testobjektet. Uppställningen lämpar sig för undervisning eftersom körningstiden är kort (1 timme) och massöverföringskoefficienten kan tas fram med linjär regression. Experimentet kan bland annat varieras genom att ändra temperatur och omrörning.

Yes / CO2 capture from natural gas was experimentally and theoretically studied using a dead-end polymeric permeation cell. A numerical model was proposed for the separation of CO2/CH4 using Polytetrafluoroethylene (PTFE) in a flat sheet membrane module and developed based upon the continuity, momentum and mass transfer equations. The slip velocity condition was considered to show the reflection of gas flow in contact with the membrane surface. The solution method was based on the well-known SIMPLE algorithm and implemented using MATLAB to determine the velocity and concentration profiles. Due to change in velocity direction in the membrane module, the hybrid differencing scheme was used to solve the diffusion-convection equation. The results of the model were compared with the experimental data obtained as part of this work and good agreement was observed. The distribution of CO2 concentration inside the feed and permeate chambers was shown and the velocity profile at the membrane surface was also determined using reflection factor for polymericmembrane. The modelling result revealed that increasing the amount of CO2 in gas feed resulted in an increase in the CO2 in the permeate stream while the gas feed pressure increased. By changing the permeability, the model developed by use of the solution-diffusion concept could be used for all polymeric membranes with flat sheet modules.

Prominin-1 (alias CD133) has received considerable interest because of its expression by several stem and progenitor cells originating from various sources, including the neural and hematopoietic systems. As a cell surface marker, prominin-1 is now used for somatic stem cell isolation. Its expression in cancer stem cells has broadened its clinical value, as it might be useful to outline new prospects for more effective cancer therapies by targeting tumor-initiating cells. Cell biological studies of this molecule have demonstrated that it is specifically concentrated in various membrane structures that protrude from the planar areas of the plasmalemma. Prominin-1 binds to the plasma membrane cholesterol and is associated with a particular membrane microdomain in a cholesterol-dependent manner. Although its physiological function is not yet determined, it is becoming clear that this cell surface protein, as a unique marker of both plasma membrane protrusions and membrane microdomains, might reveal new aspects of the cell biology of rare stem and cancer stem cells. The aim of this review is to outline the recent discoveries regarding the dynamic reorganization of the plasma membrane of rare CD133+ hematopoietic progenitor cells during cell migration and division. / Dieser Beitrag ist mit Zustimmung des Rechteinhabers aufgrund einer (DFG-geförderten) Allianz- bzw. Nationallizenz frei zugänglich.

Thesis (Ph. D.)--University of Virginia, 2008. / Title from title page. Includes bibliographical references. Also available online through Digital Dissertations.