1 - 7 |
Co-pyrolysis of lignin and low rank coal for the production of aromatic oils Byambajav E, Paysepar H, Nazari L, Xu C |
8 - 17 |
Influence of oxidizer injection angle on the entrained flow gasification of torrefied wood powder Ogren Y, Gullberg M, Wennebro J, Sepman A, Toth P, Wiinikka H |
18 - 24 |
Effect of CaO/Fe2O3 on fusion behaviors of coal ash at high temperatures Shi WJ, Kong LX, Bai J, Xu J, Li WC, Bai ZQ, Li W |
25 - 32 |
Kinetic compensation effects in the chemical reaction-controlled regime and mass transfer-controlled regime during the gasification of biochar in O-2 Alchtar MA, Zhang S, Shao X, Dang H, Liu YR, Li TT, Zhang L, Li CZ |
33 - 43 |
Excellent low temperature NH3-SCR activity over MnaCe0.3TiOx (a=0.1-0.3) oxides: Influence of Mn addition Leng XS, Zhang ZP, Li YS, Zhang TR, Ma SB, Yuan FL, Niu XY, Zhu YJ |
44 - 52 |
Influence of mesostructured alumina on the morphology of the active phase in NiWS/Al2O3 catalysts and their activity in hydrotreating of SRGO and VGO Minaev P, Nikulshina M, Mozhaev A, Maslakov K, Boldushevskii R, Nikulshin P |
53 - 60 |
Impacts of amount of chemical agent and addition of steam for activation of petroleum coke with KOH or NaOH Wu JF, Montes V, Virla LD, Hill JM |
61 - 74 |
Power-to-Gas through thermal integration of high-temperature steam electrolysis and carbon dioxide methanation - Experimental results Gruber M, Weinbrecht P, Biffar L, Harth S, Trimis D, Brabandt J, Posdziech O, Blumentritt R |
75 - 90 |
Pore structure evaluation of cementing composites blended with coal by-products: Calcined coal gangue and coal fly ash Yang J, Su Y, He XY, Tan HB, Jiang YZ, Zeng LH, Strnadel B |
91 - 96 |
Selective production and characterization of aromatic carboxylic acids from Xianfeng lignite-derived residue by mild oxidation in aqueous H2O2 solution Liu FJ, Zong ZM, Gui J, Zhu XN, Wei XY, Bai L |
97 - 114 |
A comprehensive review on laminar spherically premixed flame propagation of syngas Xie YL, Wang XJ, Bi HQ, Yuan YP, Wang JH, Huang ZH, Lei B |
115 - 131 |
Advancement in technologies for the depolymerization of lignin Agarwal A, Rana M, Park JH |
132 - 141 |
Investigation of fluctuation behavior in viscosity of coal slags used in entrained-flow gasifiers Ma YS, Wu GX, Guo QH, Liu X, Gong Y, Yu GS |
142 - 156 |
Relationship of thermal degradation behavior and chemical structure of lignin isolated from palm kernel shell under different process severities Ma ZQ, Wang JH, Zhou HZ, Zhang Y, Yang YY, Liu XH, Ye JW, Chen DY, Wang SR |
157 - 165 |
Co-processing of crude and hydrotreated pyrolysis liquids and VGO in a pilot scale FCC riser setup Wang CX, Venderbosch R, Fang YM |
166 - 174 |
Near-azeotropic volatility behavior of hydrous and anhydrous ethanol gasoline mixtures and impact on droplet evaporation dynamics Abdollahipoor B, Shirazi SA, Reardon KF, Windom BC |
175 - 186 |
Waste materials as potential catalysts for biodiesel production: Current state and future scope Marwaha A, Rosha P, Mohapatra SK, Mahla SK, Dhir A |
187 - 198 |
Methane conversion using carbon dioxide as an oxidizing agent: A review Yabe T, Sekine Y |
199 - 206 |
Direct conversion of biomass-derived carbohydrates to 5-hydroxymethylfurfural using an efficient and inexpensive manganese phosphate catalyst Xu SQ, Pan DH, Li WQ, Shen PX, Wu YF, Song XH, Zhu YL, Xu NN, Gao LJ, Xiao GM |
207 - 214 |
Effects of HZSM-5 on volatile products obtained from the fast pyrolysis of lignin and model compounds Yang HM, Norinaga K, Li J, Zhu WY, Wang HJ |
215 - 232 |
Production and utilization of fuel pellets from biomass: A review Pradhan P, Mahajani SM, Arora A |
233 - 243 |
Kinetic modeling of the direct synthesis of dimethyl ether over a CuO-ZnO-MnO/SAPO-18 catalyst and assessment of the CO2 conversion Ateka A, Erena J, Bilbao J, Aguayo AT |
244 - 251 |
Biodiesel production by transesterification in two steps: Kinetic effect or shift in the equilibrium conversion? Pisarello ML, Maquirriain M, Olalla PS, Rossi V, Querini CA |
252 - 258 |
Application of ultra-low NOx emission control for CFB boilers based on theoretical analysis and industrial practices Ke XW, Cai RX, Zhang M, Miao M, Lyu JF, Yang HR |
259 - 267 |
Efficient and green production of biodiesel catalyzed by recyclable biomass-derived magnetic acids Wang AP, Li H, Pan H, Zhang H, Xu FS, Yu ZZ, Yang S |
268 - 278 |
SCR catalyst doped with copper for synergistic removal of slip ammonia and elemental mercury Chen CM, Cao Y, Liu ST, Chen JM, Jia WB |
279 - 293 |
Corrosion evaluation of one wet desulfurization equipment - Flue gas desulfurization unit Gong Y, Yang ZG |
294 - 303 |
Sulfonated tobacco stem carbon as efficient catalyst for dehydration of C6 carbohydrate to 5-hydroxymethylfurfural in gamma-valerolactone/water Huang F, Li WZ, Liu QC, Zhang TW, An SX, Li DW, Zhu XF |
304 - 310 |
Low-temperature trace light-tar reforming in biomass syngas by atmospheric hydrogenation and hydrogenolysis Namioka T, Okudaira K, Yukumoto M, Ninomiya Y, Ito H |
311 - 317 |
Continuous production of biodiesel by the CaO-catalyzed transesterification operated with continuously stirred tank reactor Kouzu M, Fujimori A, Fukakusa R, Satomi N, Yahagi S |
318 - 330 |
Characteristics of combustion and soot formation of ethanol-gasoline blends injected by a hole-type nozzle for direct-injection spark-ignition engines Chen R, Nishida K, Shi BL |
331 - 339 |
Thermal cracking of atmospheric residue versus vacuum residue Kaminski T, Husein MM |
340 - 351 |
Implementation of novel ice-templated materials for conversion of tars from gasification product gas Hakouk K, Klotz M, Di Geronimo E, Ranieri V, Pieterse JAZ, Almansa GA, Steele AM, Thorpe S |
352 - 360 |
Effect of CaO/Na2O on slag viscosity behavior under entrained flow gasification conditions Ge ZF, Kong LX, Bai J, Chen XD, He C, Li HZ, Bai ZQ, Li P, Li W |
361 - 374 |
Numerical simulations on Oxy-MILD combustion of pulverized coal in an industrial boiler Perrone D, Castiglione T, Klimanek A, Morrone P, Amelio M |
375 - 387 |
Phase stability analysis on green methanol synthesis process from CO2 hydrogenation in water cooled, gas cooled and double cooled tubular reactors Samimi F, Feilizadeh M, Ranjbaran M, Arjmand M, Rahimpour MR |
388 - 389 |
Enhancement of the revised Klosek and McKinley method for density calculations of liquefied natural gas (LNG) over the temperature range from (100 to 135) K at pressures up to 10 MPa (vol 165, pg 19, 2017) Tietz C, Richter M, Kleinrahm R, Span R |