Experimentation minimizing transport effects

With the site-selective hole injection and the hole trapping device established, the efficiency of the hole transport between the hole donor and acceptor, especially with respect to the distance and sequence dependence, were examined. Our experiments showed that hole transport between two guanines was extremely inefficient when the intervening sequence consisted of more than 5 A-T base pairs [1]. Hole injection into the DNA n-stack using photoexcited dCNBPU was accompanied by the formation of dCNBPU anion radical. Therefore, hole transport would always compete with the back electron transfer (BET). To minimize the effect of BET, we opted for hole transport between G triplets, that are still lower in oxidation potential than G doublet. With this experimental system, we researched the effect of the bridging sequence between two G triplets on the efficiency of hole transport [2]. 

The main problem in the determination of association rates at the gas-liquid interface is the interplay of the mass transport effects and the biospecific sorption process. The experimental studies show that both effects are involved in the binding of antigen to the antibody attached to a surface. The variations of the value of the apparent adsorption rate constant with various experimental conditions reveal the importance of the nonideal effects in such experiments. To determine the effective rate of interaction, it is important both to minimize the diffusion resistances and to estimate this contribution by increasing the amount of information. Studies with varying flow rates, particle sizes, ligand densities. 

The most serious causes of error are (i) wave and peak distortion caused by excessively fast scan rates, which are themselves caused by diffusion being an inefficient mass transport mechanism, (ii) current maxima caused by convective effects as the mercury drop forms and then grows, and (iii) IR drop, i.e. the resistance of the solution being non-zero. Other causes of error can be minimized by careful experimental design. 

In crystalline semiconductors, the most common technique for the measurement of carrier mobility involves the Hall effect. However, in noncrystalline materials, experimental data are both fragmentary and anomalous (see, for example. Ref. [5]). Measured HaU mobility is typically of the order of 10 - 10 cm A /s and is frequently found to exhibit an anomalous sign reversal with respect to other properties providing information concerning the dominant charge carrier. Thus, apart from some theoretical interest, the Hall effect measurements are of minimal value in the study of macroscopic transport in amorphous semiconductors. 

Reverse-Osmosis Experiments. All reverse-osmosis experiments were performed with continuous-flow cells. Each membrane was subjected to an initial pure water pressure of 2068 kPag (300 psig) for 2 h pure water was used as feed to minimize the compaction effect. The specifications of all the membranes in terms of the solute transport parameter [(Dam/ 6)Naci]> the pure water permeability constant (A), the separation, and the product rate (PR) are given in Table I. These were determined by Kimura-Sourirajan analysis (7) of experimental reverse-osmosis data with sodium chloride solution at a feed concentration of 0.06 m unless otherwise stated. All other reverse-osmosis experiments were carried out at laboratory temperature (23-25 °C), an operating pressure of 1724 kPag (250 psig), a feed concentration of 100 ppm, and a feed flow rate >400 cmVmin. The fraction solute separation (/) is defined as follows ... 

Some authors (7, ) have used measured parameters of solute and solvent transport for calculation of membrane pore size distributions. Difficulties associated with this approach are of both experimental and theoretical nature. The experiments need to be carried out under conditions that minimize or eliminate effects of boundary phenomena (polarization) and of solute adsorption (fouling) on the measured coefficients. This is rarely done. An even more serious obstacle in this approach is the absence of quantitative and valid relations between measured transport parameters and the size parameters of a "representative pore."... 

Batch methods can be separated further into two general types, experiments that sacrifice the entire volume of an individual reactor and experiments that remove sample aliquots from a single larger reactor. Both types of experiment require that the material of interest be placed in a vessel and stirred continuously to ensure that the effect of transport processes is minimized. In the sacrificial method, at certain time during the course of an experiment, a small-volume reactor is sacrificed and used for analysis. This method eliminates the concentrating effect of removing sample aliquots however, it requires a matrix of experimental vessels to define the system. The aliquot method does restrict the number of samples able to be withdrawn from the system however, it is less labor intensive in terms of the experimental matrix and allows for easier alteration of system conditions. 

Normally the phenomena of external and internal mass transport cannot be treated as completely separate. Theoretically, separation of these two effects may be difficult, but experimentally it is quite possible to create conditions in which (a) the effect of external transport is negligible (by increasing the relative fluid velocity) or (b) the effect of internal limitation is minimal (by reducing particle size). Generally, however, both phenomena must be taken into con-... 

Third, unlike conventional methods for evaluating charge transport in pol3nmer films on electrode surfaces (19-24), there is no current flow during the data acquisition period. Thus, effects of migration and uncompensated film resistance are minimized or completely eliminated. Fourth, the theoretical model for obtaining D pp is applicable to both the semi-infinite and finite diffusion cases. Thus, unlike many other methods (19-24), it is not necessary to adjust the experimental conditions such that the semi-infinite case is obtained. 

---