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• An experimental design was used to investigate the effects of different torrefaction conditions on the properties of biomass. • Two spectrometers were simultaneously used to capture high SNR signals of continuous spectrum and characteristic spectrum. • In-situ detection of the temperature and K release concentration of torrefied biomass pellet combustion was achieved. • Changes in combustion characteristics and K release characteristics of torrefied biomass were evaluated. The orthogonal experiment designed in this paper investigated the effect of changes in experimental parameters such as biomass species, torrefaction temperature, torrefaction time, torrefaction oxygen concentration on the physicochemical properties and combustion characteristics of the torrefaction products. Two optical fiber spectrometers were used to capture the spontaneous emission spectra of the combustion flame of compressed pellets of torrefied biomass, and the in-situ measurement of pellet combustion temperature and K release concentration at high heating rate was realized by multi-spectral analysis algorithm. The experimental results indicate that for biomass, torrefaction will lead to a decrease of volatile and moisture content and an increase of fixed carbon and ash content in components, a decrease of O and H and an increase of C content in elements, a certain loss of biomass quality, an increase of high heat value, and each indicator move closer to coal. The effects of various experimental parameters on the volatile content, mass yield, high heat value increase rate and energy yield in biomass torrefaction products have similar laws, i.e., biomass species / torrefaction oxygen concentration > torrefaction temperature > torrefaction time. The mild torrefaction product pellets have a shorter ignition delay, increased volatile combustion flame height and peak temperature, longer volatile and char combustion duration, but lower peak char combustion temperature, among which the selected torrefaction products of rice straw and pine wood showed an increase in peak temperature of 0.56 % (11 K) and 0.61 % (12 K) for the volatile stage respectively, and a decrease of and 1.29 % (20 K) and 1.29 % (21 K) for the char stage respectively. In addition, the peak K release concentration during combustion of the mild torrefaction product pellets was reduced, among which the peak K release concentrations during the volatile and char stage were reduced by 43.22 % (3.89 ppm) and 52.93 % (51.55 ppm) of the rice straw torrefaction product respectively, and by 73.14 % (1.28 ppm) and 62.08 % (15.01 ppm) for the pine wood torrefaction product respectively. Biomass torrefaction products have fuel properties closer to coal, less K released from the combustion process, which have the potential to become an alternative to coal. [ABSTRACT FROM AUTHOR]

• A measurement method of K concentration is proposed based on the emission spectrum. • The temperature affected the radiation intensity of the K characteristic spectra. • The K concentration of biomass pellets was measured at different combustion stages. • The peak K release concentration of the rice straw was 110.43 ppm. Here, a calibration method using the K concentration, temperature and the characteristic spectral line radiation intensity in flame is described. In addition, a radiation function model between these three variables, I λ 766 T , C K = 0.821 · I b (λ 766 , T) · C K , was established. A Y-type optical fiber was used to connect the spectral signals from the same direction to two spectrometers. The continuous spectra in the 500–800 nm band were used for multi-spectral temperature measurements. The combination of the measured temperature and the K characteristic spectral line radiation intensity at 766 nm was used for measurements of K concentration. The temperature and equivalent ratio of the heating atmosphere were 1300 K (±20 K) and 0.786, respectively. Compared with rice straw pellet, pine wood pellet had a lower K concentration and higher combustion temperature during the entire combustion process. The peak K release concentrations of the pine wood pellet and the rice straw pellet during the volatile combustion stage were 2.09 ppm and 10.03 ppm, respectively, and the peak flame temperatures were 1774 K and 1756 K, respectively. In the char combustion stage, the peak K release concentrations were 27.83 ppm and 110.43 ppm, respectively, and the peak surface temperatures were 1287 K and 1143 K, respectively. The established function model for measuring K concentration is also applicable to the combustion diagnosis of other K-rich fuels. [ABSTRACT FROM AUTHOR]

[Display omitted] • Comprehensive mechanism explorations on plasma-based dry reforming by detailed kinetic modeling and in-situ OES measurements. • A CH 4 conversion as high as 44.76 % was achieved without catalyst at 300 °C. • Plasma kinetic model with incorporation of dynamic electron filed and thermal effects. • The formation of C 2 hydrocarbons followed a pathway of CH 4 ↔ CH 3 /CH → C 2 H 6 ↔ C 2 H 5 ↔ C 2 H 4 → C 2 H 2. Plasma-based dry reforming in an atmospheric dielectric barrier discharge (DBD) reactor has been thoroughly studied by combination of experiments and detailed kinetics simulation. With the assistances of in-situ optical emission spectroscopy (OES) measurements and reaction pathway analysis based on plasma kinetic simulation considering non-constant electric field and thermal effects, this study provided deep insights into the reaction mechanism of plasma-based dry reforming under varied feeding gas composition, gas residence time and operation temperature. A CH 4 conversion as high as 44.76 % could be achieved without catalyst at 300 °C, with an SEI of 78 J/cm3 and feeding CH 4 ratio of 50 %. Increase of feeding CH 4 proportions were found to enhance the generation of C 2 and C 3 hydrocarbons. Consistently, the OES analysis showed that the relative intensities of spectra bands induced by deexcitation of CH, CO, and C 2 also increased monotonically. With the same increment in SEI, increasing gas residence time led to larger promotions in CH 4 and CO 2 conversion, as being compared to increase of input power. The reason could be explained as that CH 4 and CO 2 molecules experienced more successive micro-discharges with a longer gas residence time, so more energy would be devoted into CH 4 /CO 2 conversion, whereas more energy was dissipated into heat as rudely increased the discharge power due to the limit of reaction time. CO 2 conversion continuously decreased with increasing gas temperature, owing to the recombination of CO and O enhanced at higher gas temperatures. Reaction pathway analysis showed that CH 4 conversion was mainly induced by electronic dissociation and ionization at the discharge stage, while CO 2 was mainly converted by recombination reaction CO 2 + CH 2 → CH 2 O + CO and also electron collision vibrational reaction e + CO 2 → e + CO 2 (v n). The formation of C 2 hydrocarbon products was supposed to follow the path of CH 4 ↔ CH 3 /CH → C 2 H 6 ↔ C 2 H 5 ↔ C 2 H 4 → C 2 H 2. [ABSTRACT FROM AUTHOR]

• Soot inception limits and its difference in coflow flames are interpreted in C/O ratio space. • Effects of Z st on soot inception are studied using kinetics analysis in C/O ratio space. • The position of chemiluminescence in C/O ratio space and the effect of Z st on it are evaluated. • Considering the low-emission combustion technology, oxy-combustion. This study investigates soot inception limits of laminar coflow diffusion flames in the carbon-to-oxygen atom (C/O) ratio space, as well as the mechanism of flame structure affecting soot inception. And chemiluminescence characteristics in flames are evaluated. Oxy-ethylene flames with the same adiabatic flame temperature (2500 K) and different stoichiometric mixture fractions (Z st , 0.3–0.6) are investigated by relocating CO 2 from oxidant to fuel. The position of soot inception and the chemiluminescence of CH*, C 2 *, and CO 2 * are measured by a hyperspectral imager. A numerical model with a detailed kinetic mechanism is used to obtain the temperature and gas-phase species concentration. The results prove that the critical C/O ratio favorable for soot inception is 0.53, and the critical temperatures on the flame centerline and sheet are 1322 K and 1632 K, respectively. The comparatively low temperature on the flame centerline can cause soot inception, as the polycyclic aromatic hydrocarbons (PAHs) concentration and residence time can guarantee the collision and cluster formation of PAHs. Although fuel pyrolysis is promoted on the flame sheet, oxygen-containing species dilutes the concentrations of fuel pyrolysis products and PAHs to limit soot inception, necessitating high temperatures for chemical bond formation. Furthermore, the mixture fraction, local C/O ratio, and net reaction and production rate are calculated, and the key reaction paths are also identified. The results demonstrate that the increase of Z st achieves the suppression of soot inception by lowering the formation of benzene and PAHs in the high C/O ratio (>0.5) zone, improving the oxygenation in the low C/O ratio (<0.5) zone, and compressing the C/O ratio space favorable for soot formation. Meanwhile, the (CH* and C 2 *) chemiluminescence zone with a C/O ratio of roughly 0.5 exists in the flame. With Z st increases, the CH* and C 2 * chemiluminescence diminishes at the flame root and enhances downstream, whereas CO 2 * chemiluminescence remains unaltered. [ABSTRACT FROM AUTHOR]