http://meetingorganizer.copernicus.org/EGU2011/EGU2011-8999.pdfBiodegradation of propylene glycol by soil bacteria
Maria Letizia Colarieti (1,2), Giuseppe Toscano (2), Rosaria Scelza (3), Maria Antonietta Rao (3), Guido Greco
(1,2)
(1) AMRA s.c.a.r.l., Napoli, Italy, (2) DIC, Università di Napoli Federico II, Napoli, Italy, (3) DiSSPAPA, Università di Napoli
Federico II, Portici, Italy
Propylene glycol (PG) is widely used as a component of deicing agents for aircrafts. Its intensive use in Northern
airports is a source of pollution for soil and groundwater even in the presence of recovery systems. Generally
PG-based deicing agents are sprayed on the aircrafts over a recovery platform where most of liquids (deicing
and melted ice) are collected to a treatment plant. Some of PG is retained by the aircraft wings where it prevents
the formation of new ice. During take-off some of PG can drain over the runway and the surrounding soil. In
winter the PG is absorbed by the snow layer on the surrounding soil. Melting of snow in spring gives rise to PG
percolation in porous soil layers and groundwater underneath. Since PG is toxic to human beings, groundwater
pollution has to be prevented.
PG is biodegradable by soil bacteria in several environmental conditions. The rate and the extent of biodegradation
can be severely limited by many factors, such as temperature, biomass concentration, availability of additional
nutrients (nitrogen and phosphorus sources) and of electron acceptors (oxygen, nitrate, sulphate, iron and
manganese oxides). Enhancing the rate and the extent of biodegradation in the porous unsaturated layer can
prevent the pollution of groundwater.
In this paper we present experimental data on the biodegradation of PG in soil slurries under aerobic and anaerobic
conditions. Soil samples from the Gardermoen Airport (Oslo, Norway) have been used as source of PG-degrading
microorganisms. The effect of addition of nutrients and electron acceptors different from oxygen has been studied.
The rate of degradation is very slow in the absence of added nutrients and follows a zero order kinetics in time
both under aerobic and anaerobic conditions. It is probably due to maintenance metabolism without biomass
growth. By addition of ammonium and phosphate the rate is notably increased and follows first-order kinetics in
time. Tentatively an explanation in terms of exponential growth of PG-degrading biomass is postulated.
By supplementing oxygen or nitrate, the methanogenic degradation of PG can be prevented, ensuring complete
mineralization to water and carbon dioxide.
I know it's a big scary word to some, but it's only an organic alcohol.process
Propylene Glycol (PG) Production and Manufacturing Process
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Commercial production of propylene glycol is by hydration of propylene oxide. Di- and tripropylene glycols, as well as small quantities of higher glycols, are also produced in the reaction.
The reaction between propylene oxide and water takes place at a temperature of 200oC and 12 bar pressure. The amount of water is controlled to favour MPG production. The reaction mixture is dehydrated by evaporation and the various glycols separated by distillation.
There is a lot of interest in producing PG from renewable resources such as glycerine. Glycerine is a byproduct in biodiesel manufacture and with the boom in biodiesel projects, much effort is being made in finding new uses for glycerine. For example, a process for converting natural glycerine to PG has been developed by the University of Missouri. The conversion rate is claimed to be about 75% efficient.
A French biochemical company, Metabolic Explorer, has been awarded a French patent for a fermentation process based on renewable resources. Archer Daniels Midland (ADM) plans to build a plant using agricultural raw materials to produce pharmaceutical and industrial grade PG.
A carbohydrate-based route to PG could result from work at Michigan State University. It has demonstrated that crude aqueous (10%) lactic acid produced by fermentation of corn starch, dextrose or other carbohydrates can be readily hydrogenated to PG in 86% selectivity at 98% conversion.