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Supercritical Fluids and Their Application to the Recycling of High-Performance Carbon Fibre Reinforced Composite Materials

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Supercritical Fluids and Their Application to the Recycling of High-Performance Carbon Fibre Reinforced Composite Materials ( supercritical-fluids-and-their-application-recycling-high-pe )

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Figure 78: Percentage mass loss with respect to the caesium carbonate concentration [Cs2CO3],T=573K,t=30min,[Resin]=32±3mgml-1,P=15.0±0.4MPa,R2 =0.995.....221 Figure 79: Phenol concentration [PhOH] with respect to caesium carbonate concentration [Cs2CO3],T=573K,t=30min,[Resin]=32±3mgml-1,P=15.0±0.4MPa,R2 =0.968.....221 Figure 80: Percentage mass loss with respect to reaction time, [EtOH] = 100 %, T = 573 K, [Cs2CO3] = 10 mg ml-1, [Resin] = 35 ± 5 mg ml-1, P = 14.7 ± 0.3 MPa, R2 = 0.990...................223 Figure 81: Phenol concentration [PhOH] with respect to reaction time, [EtOH] = 100 %, T = 576 K, [Cs2CO3] = 10 mg ml-1, [Resin] = 35 ± 5 mg ml-1, P = 14.7 ± 0.3 MPa, R2 = 0.963........223 Figure 82: Reactor residual pressure at 313 K as a function of reaction time for [EtOH] = 100 %,T=576K,[Cs2CO3]=10mgml-1,[Resin]=35±5mgml-1,P=14.7±0.3MPa,R2 =0.9661 ................................................................................................................................................ 224 Figure 83: Production of phenol as a function of percentage mass loss of epoxy resin. T = 573 K, t = 0 - 60 min, [EtOH] = 100 %, [Resin] 32 ± 3 mg ml-1, [Cs2CO3] = 10 mg ml-1, P = 15.1 ± 0.4 MPa, R2 = 0.982......................................................................................................................226 Figure 84: Percentage mass loss with respect to propanol concentration [PrOH], T = 573 K, t = 30 min, [Cs2CO3] = 10 mg ml-1, [Resin] = 33 3 mg ± ml-1, R2 = 0.975...................................227 Figure 85: Phenol concentration [PhOH] with respect to propanol concentration [PrOH], T = 573 K, t = 30 min, [Cs2CO3] = 10 mg ml-1, [Resin] = 33 3 mg ± ml-1, R2 = 0.970 .....................228 Figure 86: Reactor internal pressure as a function of temperature for varying propanol concentrations [PrOH] ...........................................................................................................229 Figure 87: Percentage mass with respect to caesium carbonate concentration [Cs2CO3], T = 573 K, t = 30 min, [Resin] = 32 ± 3 mg ml-1, P = 12.4 ± 0.4 MPa, R2 = 0.985..........................230 Figure 88: Phenol concentration [PhOH] with respect to caesium carbonate concentration [Cs2CO3],T=573K,t=30min,[Resin]=32±3mgml-1,P=12.4±0.4MPa,R2 =0.974.....231 20

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