Changes in water and ash contents in the body and calorific values of dry and wet body weight during nestling development of Pygoscelis antarctica and P. papus. were examinted. It was found that water content in the tissues of both species decreases from 85% to less than 65% whereas the content of mineral substances in dry body weight increases from 9<Vo to about 12%, at the time. Caloricity indices are high and increase during the development of nestlings. A particularly intense increase (from 0.8 kcal x g-1 to 2.2 kcal x g-1 ) characterizes calorific value of 1 gram of biomass.
The influence of sewage sludge torrefaction temperature on fuel properties was investigated. Non-lignocellulosic waste thermal treatment experiment was conducted within 1 h residence time, under the following temperatures: 200, 220, 240, 260, 280 and 300°C. Sawdust was used as lignocellulosic reference material. The following parameters of biochar have been measured: moisture, higher heating value, ash content, volatile compounds and sulfur content. Sawdust biochar has been confirmed to be a good quality solid fuel. High ash and sulfur content may be an obstacle for biochar energy reuse. The best temperature profile for sawdust torrefaction and fuel production for 1 h residence time was 220°C. At this temperature the product contained 84% of initial energy while decreased the mass by 25%. The best temperature profile for sewage sludge was 240°C. The energy residue was 91% and the mass residue was 85%. Higher temperatures in both cases caused excessive mass and energy losses.
The structure of electricity production in Poland has not changed dramatically recently. Approximately 93% of electricity is currently produced from coal and lignite. Environmental charges have a significantly impact on costs of production. This paper analyses the impact of environmental charges influenced by coal quality on the production cost of power generation. A simulation of the impact of coal quality (Q, A, S) on the environmental charges was carried out. The study was extended by the analysis based on improved relationship between coal quality and emission charges. The calculations included also charges related to the NOx, CO and CO2. The results are presented per 1 ton of coal burned and per 1 MWh of electricity produced.
The properties, superior calorific value (SCV) and the compressibility factor (z), of 77 natural gas (NG) samples are calculated from two different calibration approaches of gas chromatography, based on ISO 6974-2. The method A uses an analytical curve with seven points that the best adjust is confirmed by Analysis of Variance (ANOVA); it is required when the composition of the natural gas varies. The method B uses a single point calibration, with an allowed tolerance between the calibration gas mixture and sample mole fraction, so it is used to analyze constant natural gas streams. From natural gas composition analyzed by both methods, exceeding the method B allowed tolerance; SCV, z and its uncertainties are calculated and compared. The results show that all samples that comply with Brazilian legislation can be analyzed by method B, because there are no metrological differences in terms of SCV and z, even though the allowed tolerance has been exceeded. This simplified methodology minimizes operator exposure, besides saving about US$ 50,000.00 per chromatograph.
The new legislative provisions, regulating the solid fuel trade in Poland, and the resolutions of
provincial assemblies assume, inter alia, a ban on the household use of lignite fuels and solid fuels
produced with its use; this also applies to coal sludge, coal flotation concentrates, and mixtures
produced with their use. These changes will force the producers of these materials to find new
ways and methods of their development, including their modification (mixing with other products
or waste) in order to increase their attractiveness for the commercial power industry. The presented
paper focuses on the analysis of coal sludge, classified as waste (codes 01 04 12 and 01 04 81)
or as a by-product in the production of coals of different types. A preliminary analysis aimed at
presenting changes in quality parameters and based on the mixtures of hard coal sludge (PG SILESIA)
with coal dusts from lignite (pulverized lignite) (LEAG) has been carried out. The analysis
of quality parameters of the discussed mixtures included the determination of the calorific value,
ash content, volatile matter content, moisture content, heavy metal content (Cd, Tl, Hg, Sb, As, Pb,
Cr, Co, Cu, Mn, Ni, and W), and sulfur content. The preliminary analysis has shown that mixing
coal sludge with coal dust from lignite and their granulation allows a product with the desired quality
and physical parameters to be obtained, which is attractive to the commercial power industry.
Compared to coal sludge, granulates made of coal sludge and coal dust from lignite with or without
ground dolomite have a higher sulfur content (in the range of 1–1.4%). However, this is still an
acceptable content for solid fuels in the commercial power industry. Compared to the basic coal
sludge sample, the observed increase in the content of individual toxic components in the mixture
samples is small and it therefore can be concluded that the addition of coal dust from lignite or carbonates
has no significant effect on the total content of the individual elements. The calorific value
is a key parameter determining the usefulness in the power industry. The size of this parameter for
coal sludge in an as received basis is in the range of 9.4–10.6 MJ/kg. In the case of the examined
mixtures of coal sludge with coal dust from lignite, the calorific value significantly increases to
the range of 14.0–14.5 MJ/kg (as received). The obtained values increase the usefulness in the
commercial power industry while, at the same time, the requirements for the combustion of solid
fuels are met to a greater extent. A slight decrease in the calorific value is observed in the case of
granulation with the addition of CaO or carbonates. Taking the analyzed parameters into account,
it can be concluded that the prepared mixtures can be used in the combustion in units with flue gas
desulfurization plants and a nominal thermal power not less than 1 MW. At this stage of work no
cost analysis was carried out.
In the process of extraction and enrichment of coal waste, considerable quantities of waste material are produced, mainly the gangue and coal sludge, considered as waste or raw material. The main directions of the management development of the waste rock are the production of aggregates, the production of energy products and the liquidation works in hard coal mines and the filling of excavations. The paper proposes the extension of these activities to the use of waste material. The possibility of using aggregates or extractive waste to fill open-pit excavations has been proposed, also in areas within the reach of groundwater and the possibility of building insulation layers of waste material and the production of mixtures of hard coal sludge and sewage sludge to produce material with good energy properties. The analysis was based on the author’s own research and literature data related to selected parameters of waste material. This paper presents our own preliminary studies on the amount of combustion heat and the calorific value of coal sludge combined with other wastes such as sewage sludge. The proposed methods and actions are part of the current directions of development, but they allow the extension of the scope of use of both extractive waste and products produced on the basis of gangue or coal sludge. Due to the frequent lack of the stable composition of these materials, their current properties should be assessed each time before attempting to use them. The fact that it is important to continue research to promote existing economic use and to seek new activities or methods has been concluded.
Hard coal sludge is classified as group 01 waste or it is a by-product in the production of a hard coal with variable energy importance. Pulverized lignite is not waste but a final product of drying and the very fine pulverization of lignite with a high calorific value. The study comprised the basic material before granulation such as coal sludge (PG SILESIA) and pulverized lignite (LEAG) as well as their prepared blends after the granulation on a pipe vibration granulator designed at AGH. The pulverized lignite of the LEAG company shows a low sulfur contents. In the analyzed samples its average content (Stot d) is 0.61%. An average value of this parameter in the analyzed coal sludge samples is 0.55%. The addition of pulverized lignite does not have a significant impact on the total content of sulfur and of analyzed toxic elements (Hg, As, Cd, Cr, Co, Cu, Mn, Ni, Pb, Sb, Tl, and W) in the samples. The calorific value of coal sludge falls within the range of 11.0−12.4 MJ/kg (on a dry basis). For the coal sludge and pulverized lignite blends the calorific value clearly increases to values of 14.8−17.7 MJ/kg (on dry basis). The calorific value slightly decreases in the