Protonation of aqueous alanine by photoionization of water.

Hydronium ions produced by photolysis of water are used to study the protonation dynamics of alanine zwitterions in water. The measurements are done by UV-VIS and UV-IR femtosecond transient absorption spectroscopy on alanine in H2O and D2O. It is estimated that the reaction rate constant for the deuteration of alanine zwitterions is 4 × 1010 M-1 s-1, while the reverse process has a rate constant of 2 × 108 s-1. In addition to hydronium ions the photolysis of water yields hydrogen atoms and hydrated electrons together with hydroxyl radicals and hydroxyl ions. However, no other products resulting from reactions between aqueous alanine and the photolysis products of water are positively identified during the first 530 ps after the photolysis. Potential secondary reactions that are not observed experimentally are discussed and an upper limit is set for their yield where possible.

Toward atomic resolution diffractive imaging of isolated molecules with X-ray free-electron lasers.

We give a detailed account of the theoretical analysis and the experimental results of an X-ray-diffraction experiment on quantum-state selected and strongly laser-aligned gas-phase ensembles of the prototypical large asymmetric rotor molecule 2,5-diiodobenzonitrile, performed at the Linac Coherent Light Source [Phys. Rev. Lett.112, 083002 (2014)]. This experiment is the first step toward coherent diffractive imaging of structures and structural dynamics of isolated molecules at atomic resolution, i.e., picometers and femtoseconds, using X-ray free-electron lasers.

Bio-stabilization of drinking water in supply systems as observed in the tropics.

Changes in the bacterial quality of drinking water were examined in the supply system of tropical Dar es Salaam, Tanzania. The water treatment fulfilled WHO standard guidelines. However, the water quality allowed for significant regrowth of bacteria, demonstrating that the WHO guidelines are insufficient to check whether or not the drinking water has an acceptable regrowth potential. An experimental pipe system was examined on site. A growth model was established, based on a zero order bacterial detachment kinetics for the biofilms colonizing the inner surface of the pipes, with a release rate factor R, and a first order growth kinetics in the water flowing in the pipes with a growth rate factor µ. The rate factors were estimated to be R=1.9×10(8) m(-2) h(-1) and µ=2.5 h(-1). It was concluded that growth in the biofilm played a dominant role in the bio-stabilization processes, while the initial microbial quality of the water works water and the growth in the water phase were of minor importance. The bio-stabilization process is understood herein as the reduction in the concentration of nutrients and assimilable organic carbon in the water, and thus as the reduction of the growth potential of the water. Bacterial growth and recontamination were examined during storage at the user site. The results showed that heterotrophic bacteria grew, while faecal coliforms decayed during storage. It was concluded that the users handled the water hygienically.

Chlorine decay and bacterial inactivation kinetics in drinking water in the tropics.

The decay of free chlorine (Cl2) and combined chlorine (mostly monochloramine: NH2Cl) and the inactivation of bacteria was examined in Dar es Salaam, Tanzania. Batch experiments, pilot-scale pipe experiments and full-scale pipe experiments were carried out to establish the kinetics for both decay and inactivation, and to compare the two disinfectants for use under tropical conditions. The decay of both disinfectants closely followed first order kinetics, with respect to the concentration of both disinfectant and disinfectant-consuming substances. Bacterial densities exhibited a kinetic pattern consisting of first order inactivation with respect to the density of the bacteria and the concentration of the disinfectant, and first order growth with respect to the bacterial density. The disinfection kinetic model takes the decaying concentration of the disinfectant into account. The decay rate constant for free chlorine was 114 lg(-1)h(-1), while the decay rate constant for combined chlorine was 1.84 lg(-1)h(-1) (1.6% of the decay rate for free chlorine). The average concentration of disinfectant consuming substances in the water phase was 2.6 mg Cl2/l for free chlorine and 5.6 mg NH2Cl/l for combined chlorine. The decay rate constant and the concentration of disinfectant consuming substances when water was pumped through pipes, depended on whether or not chlorination was continuous. Combined chlorine especially could clean the pipes of disinfectant consuming substances. The inactivation rate constant λ, was estimated at 3.06×10(4) lg(-1)h(-1). Based on the inactivation rate constant, and a growth rate constant determined in a previous study, the critical concentration of free chlorine was found to be 0.08 mg Cl2/l. The critical concentration is a value below which growth rates dominate over inactivation.