This study deals with the treatment of hazardous waste landfill leachate with the help of reverse osmosis. The landfill is located in an abandoned brown coal pit in northern Bohemia. The leachate contained 7.2 g/L of dissolved inorganic salts. Among other contaminants were heavy metals, arsenic, ammonia nitrogen and associated organic pollutants, especially chlorinated compounds. A mobile membrane unit (LAB M30) equipped with a spiral wound element (FILMTEC SW30-4040), with a membrane area equaling 7.4 m2 was used for the pilot plant experiments. All experiments were carried out in batch mode. 94% conversion of the input stream into the permeate was achieved by use of a two-stage arrangement. Removal efficiencies of the monitored contaminants in the feed ranged from 94% for ammonia nitrogen to 99% for the two-valent ions. Removal efficiency for total dissolved solids was 99.3% on average. Due to varying levels of humic acids in the leachate throughout the year, fouling experiments were performed to investigate the separation process under different conditions than those used in the pilot plant. Leachates containing different concentrations of added humic acids were separated using a thin film composite on a propylene membrane. The added humic acids were obtained from samples of contaminated oxihumolite.
- MeSH
- Humic Substances MeSH
- Hazardous Waste MeSH
- Refuse Disposal methods MeSH
- Osmosis MeSH
- Publication type
- Journal Article MeSH
- Research Support, Non-U.S. Gov't MeSH
We demonstrate the tolerance of bacterial strain SM2014 to various unsustainable conditions and suggest its implication in waste water management. Its sustainability to reverse osmosis pressure (2.1 MPa) during desalination, and survival percentage of 73 % under hyperbaric conditions (pressure tension of 3.1 MPa under absolute oxygen atmosphere) confirmed its pressure tolerance. The growth of this strain at pH 9 or 10 and at 60 °C alone or in combination revealed its unique physiology as poly-extremotolerant strain. As an adaptive mechanism, the ratio of saturated to unsaturated fatty acids changed with growth conditions. Under poly-extreme condition long chain saturated fatty acid (C₁₈:₀, C₁₆:₀, C₁₄:₀, C₁₂:₀) predominated at the expense of unsaturated fatty acids. The nucleotide BLAST of 16S rRNA gene sequence of strain SM2014 with the NCBI gene bank sequences showed its close identity to Bacillus licheniformis with a similarity match of 94 %. The secretion of industrially valuable enzymes proteinase, lipase and amylase under such harsh conditions further signified potential of this strain as a source of extremozymes. Its unique characteristics underscore its relevance in waste water management.
- MeSH
- Bacillus isolation & purification classification drug effects radiation effects MeSH
- Water Purification methods MeSH
- DNA, Bacterial genetics chemistry MeSH
- Financing, Organized MeSH
- Phylogeny MeSH
- Stress, Physiological MeSH
- Hydrostatic Pressure MeSH
- Hydrogen-Ion Concentration MeSH
- Fatty Acids analysis MeSH
- Microbial Viability drug effects radiation effects MeSH
- Water Microbiology MeSH
- Molecular Sequence Data MeSH
- Osmotic Pressure MeSH
- DNA, Ribosomal genetics chemistry MeSH
- RNA, Ribosomal, 16S genetics MeSH
- Sequence Analysis, DNA MeSH
- Cluster Analysis MeSH
- Hot Temperature MeSH
Over the past few decades, reverse osmosis (RO) has been the dominant technology employed in zero liquid discharge (ZLD) systems for industrial wastewater treatment (WWT). However, RO is limited to a maximum operating salinity of about 75 g kg-1. Electrodialysis (ED) is a potentially attractive option as it can achieve much higher concentrations, thereby reducing the capacity and energy demand of the subsequent evaporation step. Feed-and-bleed experiments were undertaken on a laboratory-scale ED stack using a series of model solutions based on the most common inorganic salts with the aim of determining maximum achievable concentrations. The maximum salt concentration achievable via ED ranged between 104.2 and 267.6 g kg-1, with levels predominantly limited by water transport. In addition, a straightforward review of how ED incorporation can affect ZLD process economics is presented. The operational cost of an ED-based ZLD system for processing RO retentate was almost 20% lower than comparable processes employing high-efficiency RO and disc tubular RO. As the ED-based ZLD system appears economically preferable, and as maximum achievable concentrations greatly exceeded RO operating limits, it would appear to be a promising approach for bridging the gap between RO and evaporation, and may even eliminate the evaporation step altogether.
