Synthese von selbstaggregierenden Glycopeptidkonjugaten mit (per)fluorierten Membranankern

Für eine effektive Erkennung tumorassoziierter Kohlenhydratantigene durch das Immun-system in der Krebs¬immuntherapie ist eine multivalente Präsentation der Haptene notwendig. In der vorliegenden Arbeit wurde ein neuer Zugang zu einer solch räumlichen Konzentration der Haptene untersucht, indem MUC1-Antigene mit perfluorierten Alkylketten funktionalisiert und in einer geeigneten Lipidmatrix entmischt wurden. Perfluoralkyl-Amphiphile zeichnen sich durch eine hohe Entmischungstendenz in Alkyllipiden aus und bewirken dadurch eine Anreicherung der Erkennungsstrukturen (Haptene) in Analogie zu den natürlichen raft-Domänen auf der Zelloberfläche.rnDazu wurden zunächst verschiedene Membranankersysteme mit unterschiedlichem Fluorierungsgrad entwickelt. Beispielsweise konnte ausgehend von einem zentralen Glycerin-fragment ein Membrananker mit zwei Perfluoralkylketten hergestellt werden. Letztere wurden mittels radikalischer Perfluoralkylierung eingeführt, wobei der Fluorgehalt der Verbindung über die Kettenlänge gesteuert wurde. Daneben konnte ein weiteres Ankersystem, basierend auf der Aminosäure Lysin, synthetisiert werden, dass einen bequemen Einbau der Perfluoralkylketten durch Peptidkupplungen von entsprechenden perfluorierten Aminen bzw. perfluorierten Carbonsäuren erlaubte. In diesem Fall wurde der Fluorgehalt durch die Einführung von Alkyl- bzw. Perfluoralkylketten verändert.rnBeide Systeme konnten für erste Untersuchungen ihres Phasenverhaltens mit polaren Kopf-gruppen ausgestattet werden, wobei neben einem hydrophilen, nicht-immunogenen Triethylenglycolspacer vor allem ein TN-Antigen tragendes Dipeptid zum Einsatz kam. In Gegenwart des Matrixlipids DODAMA konnten in Langmuir-Blodgett-Untersuchungen mit diesen Verbindungen eine Entmischung und die Ausbildung mikroseparierter Bereiche nachgewiesen werden. Auch war es möglich, durch Anbindung eines Fluoreszenzfarbstoffes zu zeigen, dass solche amphiphilen Membrananker auf perfluorierten Oberflächen effektiv und dauerhaft immobilisiert werden können. Damit eröffnet diese Verbindungsklasse interessante Anwendungsmöglichkeiten in der Entwicklung von diagnostischen Microarray-Formaten.rnUm eine Anbindung der fluorierten Membrananker an den N-Terminus eines an fester Phase aufgebauten mucinanalogen Glycopeptids als antigene Einheit zu ermöglichen, wurde ein entsprechendes Ankersystem auf Basis von Glutaminsäure entwickelt. Dabei wurden an diese Verbindung neben dem TN-Antigen noch weitere komplexe tumorassoziierte Kohlenhydrat-antigene des Mucintyps angebunden, wobei der Aufbau der resultierenden amphiphilen Glycolipopeptide vollständig an der festen Phase gelang. Insgesamt konnten so mithilfe des teilfluorierten Lysinankers und des zweifach perfluorierten Glutaminsäureankers erste amphiphile Glycopeptid-Konjugate hergestellt werden, deren antigene Kopfgruppe aus einer 20 Aminosäuren umfassenden Wiederholungseinheit des Mucins MUC1 mit TN-, T- bzw. STN-Antigen-Seitenkette besteht. Derartige Verbindungen stellen reizvolle Bausteine für die Tumordiagnostik und für die Entwicklung von stabilen liposomalen Tumorvakzinen dar, da die verwendeten Perfluoralkylanker die Antigenpräsentation nicht wesentlich beeinflussen und die Bindung des Antikörpers nicht behindern. rn

Aspetti fondamentali per l'analisi cinetica di reazioni fotocatalitiche.

La conoscenza e la determinazione dell’equazione cinetica è indispensabile per lo studio, la progettazione e l’ottimizzazione di qualsiasi reattore chimico. Normalmente l’analisi cinetica viene eseguita con reattori che operano in maniera quanto più prossima a condizioni ideali in modo da rendere più facile e meno affetta da errori l’interpretazione dei risultati sperimentali. In fotocatalisi è invece di fatto impossibile realizzare, anche in presenza di una perfetta miscelazione, un sistema ideale in cui si abbia un’uniforme distribuzione di tutti i parametri che influenzano la velocità di reazione. Infatti in un reattore fotocatalitico il campo di radiazione è intrinsecamente non uniforme poiché l’assorbimento della radiazione e quindi la sua attenuazione sono necessari per l’attivazione della reazione. Pertanto l’impossibilità di realizzare un sistema fotocatalitico che operi in condizioni quanto più possibile prossime all’idealità e l’incapacità di misurare sperimentalmente i valori locali di velocità di reazione e di velocità di assorbimento dei fotoni possono rendere complessa una corretta analisi cinetica. In questo lavoro vengono studiate le modalità con cui condurre comunque una rigorosa analisi cinetica di un sistema fotocatalitico slurry, nel quale il fotocalizzatore è disperso come polvere fine in sospensione nella soluzione reagente. La reazione studiata è quella di mineralizzazione dell’acido formico. Sono stati impiegati due reattori con geometrie ed illuminazioni differenti: un reattore piano illuminato con luci LED ed un reattore anulare con lampada lineare fluorescente blacklight. È stata verificata la validità di una particolare equazione cinetica, che tiene conto dell’effetto non lineare della velocità specifica (cioè per unità di massa di catalizzatore) di assorbimento dei fotoni e delle concentrazioni del reagente, dell’ossigeno e del fotocatalizzatore. Sono state inoltre determinate le condizioni critiche che possono portare ad errori nell’analisi cinetica ed è stata dimostrata l’utilità di un modello matematico che tiene conto dei bilanci di energia raggiante, di materia nonché del campo di moto. Il modello matematico, in cui compare un solo parametro aggiustabile (il tempo caratteristico di reazione od equivalentemente la costante cinetica), è in grado di riprodurre molto soddisfacentemente i risultati sperimentali in tutte le diverse condizioni operative: diversa geometria di reattore, diversa illuminazione, differente spessore ottico, diverse contrazioni di substrato e di fotocatalizzatore. Infine è stato mostrato come l’equazione cinetica ad una sola costante cinetica, che è stata adottata, descriva meglio la cinetica della reazione fotocatalitica in esame di altre equazioni a due o più costanti cinetiche spesso utilizzate in fotocatalisi e basate sulla teoria di Langmuir-Hinshelwood, a dimostrazione di un diverso meccanismo di reazione.

Characterization of hydrothermal carbonization products from woodchip

L’idrotermocarbonizzazione è un processo che permette di convertire un’elevata quantità di materie prime solide in carbone. Ciò viene realizzato inserendo come sostanza in input, oltre alla materia prima iniziale, acqua liquida e, successivamente, riscaldando fino a 180°C, temperatura alla quale inizia la reazione esotermica ed il processo diventa di tipo stand-alone. Tale reazione presenta un tempo di reazione variabile nel range di 4÷12 h. I prodotti in uscita sono costituiti da una sostanza solida che ha le caratteristiche del carbone marrone naturale e un’acqua di processo, la quale è altamente inquinata da composti organici. In questo elaborato viene illustrata una caratterizzazione dei prodotti in uscita da un impianto di idrotermo carbonizzazione da laboratorio, il quale utilizza in input pezzi di legno tagliati grossolanamente. Inizialmente tale impianto da laboratorio viene descritto nel dettaglio, dopodiché la caratterizzazione viene effettuata attraverso DTA-TGA dei materiali in ingresso ed uscita; inoltre altre sostanze vengono così analizzate, al fine di confrontarle col char ed i pezzi di legno. Quindi si riporta anche un’analisi calorimetrica, avente l’obiettivo di determinare il calore di combustione del char ottenuto; attraverso questo valore e il calore di combustione dei pezzi di legno è stato possibile calcolare l’efficienza di ritenzione energetica del processo considerato, così come la densificazione energetica riscontrata nel materiale in uscita. In aggiunta, è stata eseguita un’analisi delle specie chimiche elementari sul char ed il legno in modo da determinare i seguenti parametri: fattori di ritenzione e fattori di ritenzione pesati sulla massa in termini di concentrazione di C, H, N e S. I risultati ottenuti da tale analisi hanno permesso di effettuare una caratterizzazione del char. Un tentativo di attivazione del char viene riportato, descrivendo la procedura di attivazione seguita e la metodologia utilizzata per valutare il buon esito o meno di tale tentativo di attivazione. La metodologia consiste di uno studio isotermo dell’adsorbimento di acido acetico sul char “attivato” attraverso una titolazione. I risultati sperimentali sono stati fittati usando le isoterme di Langmuir e Freundlich e confrontati con le capacità di adsorbimento del semplice char e di un campione di carbone attivo preso da un’azienda esterna. Infine si è considerata l’acqua di processo, infatti un’analisi fotometrica ne ha evidenziato le concentrazioni di TOC, COD, ioni nitrato e ioni fosfato. Questi valori sono stati conseguentemente confrontati con i limiti italiani e tedeschi massimi ammissibili per acque potabili, dando quindi un’idea quantitativa della contaminazione di tale acqua di processo.

pH-dependent distribution of chlorin e6 derivatives across phospholipid bilayers probed by NMR spectroscopy

The pH-dependent membrane adsorption and distribution of three chlorin derivatives, chlorin e6 (CE), rhodin G7 (RG), and monoaspartyl-chlorin e6 (MACE), in the physiological pH range (pH 6-8) were probed by NMR spectroscopy. Unilamellar vesicles consisting of dioleoyl-phosphatidyl-choline (DOPC) were used as membrane models. The chlorin derivatives were characterized with respect to their aggregation behavior, the pK(a) values of individual carboxylate groups, the extent of membrane adsorption, and their flip-flop rates across the bilayer membrane for pH 6-8. External membrane adsorption was found to be lower for RG than for CE and MACE. Both electrostatic interactions and the extent of aggregation seemed to be the main determinants of membrane adsorption. Rate constants for chlorin transfer across the membrane were found to correlate strongly with the pH of the surrounding medium, in particular, for CE and RG. In acidic solution, CE and RG transfer across the membrane was strongly accelerated, and in basic solution, all compounds were retained, mostly in the outer monolayer. In contrast, MACE flip-flop across the membrane remained very low even at pH 6. The protonation of ionizable groups is suggested to be a major determinant of chlorin transfer rates across the bilayer. pK(a) values of CE and RG were found to be between 6 and 8, and two of the carboxylate groups in MACE had pK(a) values below 6. For CE and RG, the kinetic profiles at acidic pH indicated that the initial fast membrane distribution was followed by secondary steps that are discussed in this article.

Wetting and spreading of a surfactant film on solid particles: influence of sharp edges and surface irregularities

In addition to particle size and surface chemistry, the shape of particles plays an important role in their wetting and displacement by the surfactant film in the lung. The role of particle shape was the subject of our investigations using a model system consisting of a modified Langmuir-Wilhelmy surface balance. We measured the influence of sharp edges (lines) and other highly curved surfaces, including sharp corners or spikes, of different particles on the spreading of a dipalmitoylphosphatidyl (DPPC) film. The edges of cylindrical sapphire plates (circular curved edges, 1.65 mm radius) were wetted at a surface tension of 10.7 mJ/m2 (standard error (SE) = 0.45, n = 20) compared with that of 13.8 mJ/m2 (SE = 0.20, n = 20) for cubic sapphire plates (straight linear edges, edge length 3 mm) (p < 0.05). The top surfaces of the sapphire plates (cubic and cylindrical) were wetted at 8.4 mJ/m2 (SE = 0.54, n = 20) and 9.1 mJ/m2 (SE = 0.50, n = 20), respectively, but the difference was not significant (p > 0.05). The surfaces of the plates showed significantly higher resistance to spreading compared to that of the edges, as substantially lower surface tensions were required to initiate wetting (p < 0.05). Similar results were found for talc particles, were the edges of macro- and microcrystalline particles were wetted at 7.2 mJ/m2 (SE = 0.52, n = 20) and 8.2 mJ/m2 (SE = 0.30, n = 20) (p > 0.05), respectively, whereas the surfaces were wetted at 3.8 mJ/m2 (SE = 0.89, n = 20) and 5.8 mJ/m2 (SE = 0.52, n = 20) (p < 0.05), respectively. Further experiments with pollen of malvaceae and maize (spiky and fine knobbly surfaces) were wetted at 10.0 mJ/m2 (SE = 0.52, n = 10) and 22.75 mJ/m2 (SE = 0.81, n = 10), respectively (p < 0.05). These results show that resistance to spreading of a DPPC film on various surfaces is dependent on the extent these surfaces are curved. This is seen with cubic sapphire plates which have at their corners a radius of curvature of about 0.75 microm, spiky malvaceae pollen with an even smaller radius on top of their spikes, or talc with various highly curved surfaces. These highly curved surfaces resisted wetting by the DPPC film to a higher degree than more moderately curved surfaces such as those of cylindrical sapphire plates, maize pollens, or polystyrene spheres, which have a surface free energy similar to that of talc but a smooth surface. The macroscopic plane surfaces of the particles demonstrated the greatest resistance to spreading. This was explained by the extremely fine grooves in the nanometer range, as revealed by electron microscopy. In summary, to understand the effects of airborne particles retained on the surfaces of the respiratory tract, and ultimately their pathological potential, not only the particle size and surface chemistry but also the particle shape should be taken in consideration.

EVALUATION OF MAGNESIUM AS A HALL THRUSTER PROPELLANT

In this study, the use of magnesium as a Hall thruster propellant was evaluated. A xenon Hall thruster was modified such that magnesium propellant could be loaded into the anode and use waste heat from the thruster discharge to drive the propellant vaporization. A control scheme was developed, which allowed for precise control of the mass flow rate while still using plasma heating as the main mechanism for evaporation. The thruster anode, which also served as the propellant reservoir, was designed such that the open area was too low for sufficient vapor flow at normal operating temperatures (i.e. plasma heating alone). The remaining heat needed to achieve enough vapor flow to sustain thruster discharge came from a counter-wound resistive heater located behind the anode. The control system has the ability to arrest thermal runaway in a direct evaporation feed system and stabilize the discharge current during voltage-limited operation. A proportional-integral-derivative control algorithm was implemented to enable automated operation of the mass flow control system using the discharge current as the measured variable and the anode heater current as the controlled parameter. Steady-state operation at constant voltage with discharge current excursions less than 0.35 A was demonstrated for 70 min. Using this long-duration method, stable operation was achieved with heater powers as low as 6% of the total discharge power. Using the thermal mass flow control system the thruster operated stably enough and long enough that performance measurements could be obtained and compared to the performance of the thruster using xenon propellant. It was found that when operated with magnesium, the thruster has thrust ranging from 34 mN at 200 V to 39 mN at 300 V with 1.7 mg/s of propellant. It was found to have 27 mN of thrust at 300 V using 1.0 mg/s of propellant. The thrust-to-power ratio ranged from 24 mN/kW at 200 V to 18 mN/kW at 300 volts. The specific impulse was 2000 s at 200 V and upwards of 2700 s at 300 V. The anode efficiency was found to be ~23% using magnesium, which is substantially lower than the 40% anode efficiency of xenon at approximately equivalent molar flow rates. Measurements in the plasma plume of the thruster—operated using magnesium and xenon propellants—were obtained using a Faraday probe to measure off-axis current distribution, a retarding potential analyzer to measure ion energy, and a double Langmuir probe to measure plasma density, electron temperature, and plasma potential. Additionally, the off axis current distributions and ion energy distributions were compared to measurements made in krypton and bismuth plasmas obtained in previous studies of the same thruster. Comparisons showed that magnesium had the largest beam divergence of the four propellants while the others had similar divergence. The comparisons also showed that magnesium and krypton both had very low voltage utilization compared to xenon and bismuth. It is likely that the differences in plume structure are due to the atomic differences between the propellants; the ionization mean free path goes down with increasing atomic mass. Magnesium and krypton have long ionization mean free paths and therefore require physically larger thruster dimensions for efficient thruster operation and would benefit from magnetic shielding.

Time-dependent interactions of the two porphyrinic compounds chlorin e6 and mono-L-aspartyl-chlorin e6 with phospholipid vesicles probed by NMR spectroscopy

The distribution processes of chlorin e6 (CE) and monoaspartyl-chlorin e6 (MACE) between the outer and inner phospholipid monolayers of 1,2-dioleoyl-phosphatidylcholine (DOPC) vesicles were monitored by 1H NMR spectroscopy through analysis of chemical shifts and line widths of the DOPC vesicle resonances. Chlorin adsorption to the outer vesicle monolayer induced changes in the DOPC 1H NMR spectrum. Most pronounced was a split of the N-methyl choline resonance, allowing for separate analysis of inner and outer vesicle layers. Transbilayer distribution of the chlorin compounds was indicated by time-dependent characteristic spectral changes of the DOPC resonances. Kinetic parameters for the flip-flop processes, that is, half-lives and rate constants, were obtained from the experimental data points. In comparison to CE, MACE transbilayer movement was significantly reduced, with MACE remaining more or less attached to the outer membrane layer. The distribution coefficients for CE and MACE between the vesicular and aqueous phase were determined. Both CE and MACE exhibited a high affinity for the vesicular phase. For CE, a positive correlation was found between transfer rate and increasing molar ratio CE/DOPC. Enhanced membrane rigidity induced by increasing amounts of cholesterol into the model membrane was accompanied by a decrease of CE flip-flop rates across the membrane. The present study shows that the movement of porphyrins across membranes can efficiently be investigated by 1H NMR spectroscopy and that small changes in porphyrin structure can have large effects on membrane kinetics.

Proceedings of the Fifth Biochemical Engineering Symposium

This report presents the proceedings of the Biochemical Engineering Symposium held at Kansas State University, April 26, 1975. Since a number of the contributions will be published in detail elsewhere, only brief summaries of each contribution are included here. Requests for additional information on projects conducted at Iowa State University should be directed to Dr. Peter J. Reilly, and those at Kansas State University to the editors. Contents"Enzymatic Breakdown of Hemicellulose," Alfred R. Fratzke, Iowa State University "Biochemical Aspects of Hydrocarbon Uptake in Hydrocarbon Fermentations," Tadaatsu Nakahara, Kansas State University "Optimal Concentration Profiles for Bifunctional Catalysts with Langmuir-Hinshelwood Kinetics and Varying Effectiveness Factors," Ho Nam Chang, Iowa State University "Single Cell Protein Production from Hydrocarbons in Tower Systems," J. R. Gutierrez, Kansas State University "Effect of Temperature and pH on the Stability and Activity of Immobilized Glucoamylase and Glucose Isomerase," Gene K. Lee, Iowa State University "Oxygen Transfer in a Tower System with Two Liquid Phases," G. T. MacLean, Kansas State University "Continuous Production of Glucose from Dextrin by Glucoamylase Immlobilized on Porous Silica," Douglas D. Lee, Iowa State University

Nebulizing poractant alfa versus conventional instillation: Ultrastructural appearance and preservation of surface activity.

BACKGROUND Nebulized surfactant therapy has been proposed as an alternative method of surfactant administration. The use of a perforated vibrating membrane nebulizer provides a variety of advantages over conventional nebulizers. We investigated the molecular structure and integrity of poractant alfa pre- and post-nebulization. METHOD Curosurf® was nebulized using an Investigational eFlow® Nebulizer System. Non-nebulized surfactant ("NN"), recollected surfactant droplets from nebulization through an endotracheal tube ("NT") and nebulization of surfactant directly onto a surface ("ND") were investigated by transmission electron microscopy. Biophysical characteristics were assessed by the Langmuir-Wilhelmy balance and the Captive Bubble Surfactometer. RESULTS Volume densities of lamellar body-like forms (LBL) and multi-lamellar forms (ML) were high for "NN" and "NT" samples (38.8% vs. 47.7% for LBL and 58.2% vs. 47.8% for ML). In the "ND" sample, we found virtually no LBL's, ML's (72.6%) as well as uni-lamellar forms (16.4%) and a new structure, the "garland-like" forms (9.4%). Surface tension for "NN" and "NT" was 23.33 ± 0.29 and 25.77 ± 1.12 mN/m, respectively. Dynamic compression-expansion cycling minimum surface tensions were between 0.91 and 1.77 mN/m. CONCLUSION The similarity of surfactant characteristics of nebulized surfactant via a tube and the non-nebulized surfactant suggests that vibrating membrane nebulizers are suitable for surfactant nebulization. Alterations in surfactant morphology and characteristics after nebulization were transient. A new structural subtype of surfactant was identified. Pediatr Pulmonol. 2014; 49:348-356. © 2013 Wiley Periodicals, Inc.