Effects of torrefaction on product distribution and quality of bio-oil from food waste pyrolysis in N2 and CO2.

Waste food utilization to produce bio-oil through pyrolysis has received increasing attention. The feedstock can be utilized more efficiently as its properties are upgraded. In this work, the mixed food waste (MFW) was pretreated via torrefaction at moderate temperatures (250-275 °C) under an inert atmosphere before fast pyrolysis. The pyrolysis of torrified MFW (T-MFW) was performed in a bubbling fluidized-bed reactor (FBR) to study the influence of torrefaction on the pyrolysis product distribution and bio-oil compositions. The highest liquid yield of 39.54 wt% was observed at a pyrolysis temperature of 450℃. The torrefaction has a significant effect on the pyrolysis process of MFW. After torrefaction, the higher heating values (HHVs) of the pyrolysis bio-oils (POs) ranged from 31.51 to 34.34 MJ/kg, which were higher than those of bio-oils from raw MFW (27.69-31.58 MJ/kg). The POs mainly contained aliphatic hydrocarbons (alkenes and ketones), phenolic, and N-containing derivatives. The pyrolysis of T-MFW was also carried out under the CO2 atmosphere. The application of CO2 as a carrier gas resulted in a decrease in the liquid yield and an increase in the gas product yield. In addition, the carbon and nitrogen content of POs increased, whereas the oxygen was reduced via the release of moisture and CO. Using CO2 in pyrolysis inhibited the generation of nitriles derivatives in POs, which are harmful to the environment. These results indicated that the application of CO2 to the thermal treatment of T-MFW could be feasible in energy production as well as environmental pollution control.

Catalytic upgrade for pyrolysis of food waste in a bubbling fluidized-bed reactor.

Biofuel production via pyrolysis has received increasing interest as a promising solution for utilization of now wasted food residue. In this study, the fast pyrolysis of mixed food waste (MFW) was performed in a bubbling fluidized-bed reactor. This was done under different operating conditions (reaction temperatures and carrier gas flow rate) that influence product distribution and bio-oil composition. The highest liquid yield (49.05 wt%) was observed at a pyrolysis temperature of 475 °C. It was also found that the quality of pyrolysis bio-oils (POs) could be improved using catalysts. The catalytic fast pyrolysis of MFW was studied to upgrade the pyrolysis vapor, using dolomite, red mud, and HZSM-5. The higher heating values (HHVs) of the catalytic pyrolysis bio-oils (CPOs) ranged between 30.47 and 35.69 MJ/kg, which are higher than the HHVs of non-catalytic pyrolysis bio-oils (27.69-31.58 MJ/kg). The major components of the bio-oils were fatty acids, N-containing compounds, and derivatives of phenol. The selectivity for bio-oil components varied depending on the catalysts. In the presence of the catalysts, the oxygen was removed from oxygenates via moisture, CO2, and CO. The CPOs contained aliphatic hydrocarbons, polycyclic aromatic compounds (such as naphthalene), pyridine derivatives, and light oxygenates (cyclic alkenes and ketones).

Production of bio-oil from fast pyrolysis of biomass using a pilot-scale circulating fluidized bed reactor and its characterization.

To circumvent the adverse impacts arising from an excessive use of fossil fuels, bioenergy and chemical production from a carbon neutral resource (biomass) has drawn considerable attention over the last two decades. Among various technical candidates, fast pyrolysis of biomass has been considered as one of the viable technical routes for converting a carbonaceous material (biomass) into biocrude (bio-oil). In these respects, three biomass samples (i.e., sawdust, empty fruit bunch, and giant Miscanthus) were chosen as a carbon substrate for the pyrolysis process in this study. A pilot-scale circulating fluidized bed reactor was employed for the pyrolysis work, and biocrude from the fast pyrolysis process at 500 °C were characterized because the maximum yield of biocrude (60 wt% of the original sample mass) was achieved at 500 °C. The physico-chemical properties of biocrude were measured by the international standard/protocol (ASTM D7544 and/or EN 16900 test method) to harness biocrude as bioenergy and an initial feedstock for diverse chemicals. All measurements in this study demonstrated that the heating value, moisture content, and ash contents in biocrude were highly contingent on the type of biomass. Moreover, characterization of biocrude in this study significantly suggested that additional unit operations for char and metal removal must be conducted to meet the fuel standard in terms of biocrude as bioenergy.

A DNA immunoprecipitation assay used in quantitative detection of in vitro DNA-protein complex binding.

To begin gene transcription, several transcription factors must bind to specific DNA sequences to form a complex via DNA-protein interactions. We established an in vitro method for specific and sensitive analyses of DNA-protein interactions based on a DNA immunoprecipitation (DIP) method. We verified the accuracy and efficiency of the DIP assay in quantitatively measuring DNA-protein binding using transcription factor CP2c as a model. With our DIP assay, we could detect specific interactions within a DNA-CP2c complex, with reproducible and quantitative binding values. In addition, we were able to effectively measure the changes in DNA-CP2c binding by the addition of a small molecule, FQI1 (factor quinolinone inhibitor 1), previously identified as a specific inhibitor of this binding. To identify a new regulator of DNA-CP2c binding, we analyzed several CP2c binding peptides and found that only one class of peptide severely inhibits DNA-CP2c binding. These data show that our DIP assay is very useful in quantitatively detecting the binding dynamics of DNA-protein complex. Because DNA-protein interaction is very dynamic in different cellular environments, our assay can be applied to the detection of active transcription factors, including promoter occupancy in normal and disease conditions. Moreover, it may be used to develop a targeted regulator of specific DNA-protein interaction.

Heat processing decreases Amadori products and increases total phenolic content and antioxidant activity of Korean red ginseng.

The functional properties of Korean red ginseng (KRG) are known to be dependent upon the extent of heat processing. We demonstrated that repeated heat processing in the preparation of KRG decreased its arginyl-fructosyl-glucose (AFG) content and metal chelating capacity. On the other hand, the total phenolic compound content, in vitro peroxyl radical scavenging ability, and cellular peroxyl and hydroxyl radical scavenging ability increased with repeated heat processing. The peroxyl radical scavenging ability of KRG may be due to the total phenolic compound content. The hydroxyl radical scavenging ability of KRG seems to result mainly from the chelating ability of Amadori compounds such as arginyl-fructose and AFG. The protective ability of KRG against Cu²(+)-induced oxidative stress in hepatoma HepG2 cells may be due to permeability into the cell membrane rather than antioxidant activity. These results can be used to predict the physiological functions of KRG in in vivo models.