The low-temperature Fischer-Tropsch synthesis (LTFT) processing of renewable feedstocks combined with the hydrocracking of its solid product is an effective way to produce synthetic renewable engine fuels. The hydrocracking of an FT wax derived from natural gas using the LTFT synthesis was studied in this paper. The hydrocracking was carried out in a tubular fixed-bed reactor with a cocurrent flow of the feedstock and hydrogen. Reaction temperatures in the range of 305– 370 °C, a pressure of 8 MPa, an H2/feed ratio of 500 m3/m3 and weight hour space velocities (WHSV) of 1; 2 and 4 h-1 were tested. The naphtha fraction (boiling up to 200 °C) was the main product of the hydrocracking under all the tested reaction conditions. It could be used as a component into petroleum-derived gasoline in a neat form or the after processing by common refinery processes (isomerization and/or reforming). The production of low-sulfur and low-aromatic paraffinic solvent or the utilization as a feedstock for steam cracking could be some other options of the naphtha fraction utilization. The maximum yield of the gaseous products (depending on the reaction temperatures and WHSV) was 20 wt.%. They were primarily composed of n-alkanes and isoalkanes and could be, therefore, used as an optimal feedstock for steam cracking as well. The C3-C4 fraction of the gaseous products could be also utilized as an LPG fuel. Very low yields (up to 10.4 wt.%) of the middle distillates were obtained under all the tested reaction conditions. Due to their saturated nature, their densities were very low and, additionally, poor low-temperature properties can be expected.
The reliance on solid fuels for heat processing and power generation with low efficiency and inadequately control of gaseous pollutants is strongly related to health impacts and environmental pollution. Atmospheric dispersion modelling is an essential tool to assess the potential impacts of related stationary sources on local air quality. Advanced Gaussian plume models provide an up-to-date assemble of algorithms to estimate contaminant concentrations distributed at a variety of heights and distances. This review presented a comparative evaluation on ADMS and AERMOD performance in different validation scenarios considering SO2 emissions and the NOx chemistry scheme. Terrain, stack height and plume rise influence on emissions, along with modelling uncertainties and limitations were also discussed. Contour plots of maximum daily values and annual averages confirmed a remarkable similarity in patterns within simulations. By this approach, the study extended recent practical information and recommended a complementary instrument for the improvement of the reference model SYMOS´97 implemented in the Czech Republic.
The hydrotreating of vegetable oils and animal fats is a possible way to produce a high-quality renewable diesel fuel component. It can be produced by processing the bio-raw material in new units or by the co-pro-cessing of the renewable raw material together with the petroleum middle distillates in existing hydrotreating units. This work was focused on investigating the effect of the hydrogen to the feedstock ratio on the hydrotreating of a mixture of petroleum middle distillates and rapeseed oil in a weight ratio of 8:2 in a tubular fixed-bed reactor. The hydrotreating was performed using a sulfided Ni-Mo/Al2O3 catalyst, a temperature of 345 °C, a WHSV of 1.0 h-1, a pressure of 4.0 MPa and a hydrogen to the feedstock ratio in the range of 120-600 m3∙m-3. The hydrogen to feedstock ratio of 120 m3∙m-3 was not sufficient to desulfurise the feedstock to the level of 10 mg∙kg-1. On the contrary, increasing the hydrogen to feedstock ratio to above 240 m3∙m-3 had no significant effect on the yield and quality of the obtained products. Therefore, the ratio of 240 m3∙m-3 was considered as sufficient for the hydrotreating of the mixture of the petroleum middle distillates and rapeseed oil.
The stability of marine fuels is traditionally a very hot topic, especially in the beginning of so-called sulphur cap. The sulphur cap is the process of reducing the maximum level of sulphur content (from 3.5 to 0.5 wt%) in marine fuels, which are being used on deep sea from the first of January 2020. After this change, the large amount of marine fuels will be produced as a mixture of two or more components to achieve required sulphur level. Higher amounts of cutter stocks will increase the likelihood of decreased stability or compatibility of the marine fuels. Therefore, a reliable stability tests or their combination will be very important for marine fuels evaluation. However, only total sediment after aging is defined as a standard method according to ISO 8217 for stability testing. This method is not suitable for all the analysed marine fuels, so we verified using of microscopy for this type of evaluation. The set of marine fuels samples was tested using microscopy, results were processed and correlated with other selected qualitative parameters. The microscopy was evaluated as a suitable method for testing of marine fuels stability. This method could be used for very fast evaluation in industrial as well as research laboratories in combination with standard methods.