Advances in Environmental Research : Volume 58

In Chapter One, Alexander M. Liudchik and Siarhey D. Umreika begin by deliberating on the problem of spectrophotometric determination of gas medium composition in its customary formulation and then define a method of accounting for the errors from different sources, thus allowing for estimation of uncertainties in the contents of individual components.

In Chapter Two, Oleg V. Trifonov and Vladimir P. Cherniy give an overview of current research on the pipeline-soil interaction modeling, examine a variety of modeling approaches, and describe the environment for correct application of different soil models.

In Chapter Three, Alexander Y. Galashev studies the spectral properties of clusters of water that have absorbed NOx molecules.

Next, Dr. Francis Orata recommends two consecutive points of sewage and wastewater treatment, including dispersed treatment at the pollutant production facility or at the source, during Chapter Four.

In Chapter Five, G. Lovato, R. Albanez, J.N. Albuquerque, P. Cola, R.S. Celestino, S.E. Vogel, M. Fukuyama, F.E. Hirata, F.H. Saito, S.M. Ratusznei, and J.A.D. Rodrigues explore the application of an AnSBBR (anaerobic sequencing batch biofilm reactor) of 3.0 L treating 1.0 L per cycle with agitation operated at 30 DegreesC in batch and fed-batch mode in the co-digesting cheese whey with glycerin for methane production.

In Chapter Six, Bingqi Zhu researches the chemical weathering process of detrital sediments in the hyper-arid area, basing his study on major-element components of deposits from the Taklamakan Desert in China.

After, J. F. Perez, J. Llanos, C. Saez, C. Lopez, M. A. Rodrigo, and P. Canizares present a study using 100 different samples collected from a variety of manufacturing processes within a chemical synthesis pharmaceutical manufacturing plant in Chapter Seven.

Lastly, Chapter Eight presents a study investigating the application of an anaerobic sequencing batch biofilm reactor of .0 L treating 1.0 L per cycle with recirculation of the liquid phase operated at 30 DegreesC in batch and fed-batch mode in the treatment of xylose based wastewater, with the core intent of producing methane.