[1]SANGHAVI R R, KAMALE P J, SHAIKH M A R, et al. HMX based enhanced energy LOVA gun propellant[J]. Journal of Hazardous Materials, 2007, 143(1/2): 532-534.[2]PANG W Q, DE LUCA L T, XU H X, et al. Effects of CL-20 on the properties of glycidyl azide polymer (GAP) solid rocket propellant[J]. International Journal of Energetic Materials and Chemical Propulsion, 2016, 15(1): 49-64.
[3]ZHOU K, HE Z Q, YIN S P, et al. Numerical simulation for exploring the effect of viscosity on single-screw extrusion process of propellant[J]. Procedia Engineering, 2014, 84: 933-939.
[4]DOMBE G, MAURYA M, BHONGALE C. Application of twin screw extrusion for continuous processing of energetic materials[J]. Central European Journal of Energetic Materials, 2015, 12(3): 507-522.
[5]徐俊杰, 张先明, 陈文兴,等. 微型锥形双螺杆挤出机混合性能的数值模拟[J]. 高分子材料科学与工程, 2015,31(3):128-132.
XU J J, ZHANG X M, CHEN W X, et al. Numerical simulation of mixing performance in the miniature conical twin screw extruder[J]. Polymer Materials Science and Engineering, 2015,31(3):128-132.
[6]YANG K X, XIN C L, YU D Q, et al. Numerical simulation and experimental study of pressure and residence time distribution of triple-screw extruder[J]. Polymer Engineering & Science, 2015,55(1):156-162.
[7]PONOMAREV D, RODIER E, SAUCEAU M, et al. Modelling non-homogeneous flow and residence time distribution in a single-screw extruder by means of Markov chains[J]. Journal of Mathematical Chemistry, 2012,50(8):2141-2154.
[8] REITZ E, PODHAISKY H, ELY D, et al. Residence time modeling of hot melt extrusion processes[J]. European Journal of Pharmaceutics & Biopharmaceutics, 2013,85(3):1200-1205.
[9] DING Y J,WEI R J,YING S J.In-line rheological behaviors of gun propellant substitute assisted with supercritical CO2 in extrusion processing[J]. Propellants,Explosives,Pyrotechnics,2017,42(3):247252.
[10]CURIA S, DE FOCATIIS D S A, HOWDLE S M. High-pressure rheological analysis of CO2-induced melting point depression and viscosity reduction of poly(ε-caprolactone)[J]. Polymer, 2015, 69: 17-24.
[11] FRANKEN H H, KNOETZE J H, SCHWARZ C E. High-pressure binary phase equilibria, density and dynamic viscosity of 100 & 200 cSt polydimethylsiloxane (PDMS) with supercritical CO2[J]. The Journal of Supercritical Fluids, 2018, 139: 1-7.
[12]KLOZI-SKI A. The application of an extrusion modular slit head of a special construction in the inline extensional viscosity measurements of polymers[J]. Polymer Testing, 2019, 73: 186-192.
[13]YEH A I, JAW Y M. Predicting residence time distributions in a single screw extruder from operating conditions[J]. Journal of Food Engineering, 1999, 39(1): 81-89.
[14]BOCHMANN E S, STEFFENS K E, GRYCZKE A, et al. Numerical simulation of hot-melt extrusion processes for amorphous solid dispersions using model-based melt viscosity[J]. European Journal of Pharmaceutics and Biopharmaceutics, 2018, 124: 34-42.
[15]AVELINO H M N T, FARELEIRA J M N A, GOURGOUILLON D, et al. Viscosity of poly(ethyleneglycol) 200 [PEG 200] saturated with supercritical carbon dioxide[J]. The Journal of Supercritical Fluids, 2017, 128: 300-307.