Plastics Process Analysis, Instrumentation, and Control. Группа авторов

C₂H₆ 3.6 3.1 C₂H₄ 33.1 29.9 C₂H₂ 0.4 0.5 C₃H₈ 0.4 0.4 C₃H₆ 16.8 15.2 Propyne 0.2 0.3 Propadiene 0.3 0.4 i–C₄H₁₀ 0.0 0.0 n–C₄H₁₀ 0.1 0.2 1-Butene 2.1 1.4 i-Butene 0.7 2.1 2-Butene (c) 0.5 0.5 2-Butene (t) 0.4 0.3 C₄H₆ 7.2 4.9 C₅HC 5.2 4.5 C₆–C₈NA 1.8 2.1 Benzene 7.8 7.9 Toluene 2.9 3.5 EB + Xylenes 0.6 1.1 Styrene 0.8 1.0 C₉HC 0.7 0.9 C₁₀ + HC 3.0 4.0

Table 1.8 Cracked products from liquid material and naphtha (93).

Compound	Steam cracker Amount/[%]	Naphtha Amount/[%]
CO	0.2	0.2
H2	1.0	1.0
CH4	16.8	14.6
C2H6	6.5	3.1
C2H4	31.8	29.9
C2H2	0.7	0.5
C3H8	3.2	0.4
C3H6	16.1	15.2
Propyne	0.3	0.3
Propadiene	0.5	0.4
i–C4H10	0.0	0.0
n–C4H10	1.0	0.2
1-Butene	1.0	1.4
i-Butene	0.9	2.1
2-Butene (c)	0.4	0.5
2-Butene (t)	0.3	0.3
C4H6	4.9	4.9
C5HC	2.6	4.5
C6–C8NA	0.5	2.1
Benzene	6.0	7.9
Toluene	1.7	3.5
EB + Xylenes	0.3	1.1
Styrene	0.6	1.0
C9HC	0.3	0.9
C10 + HC	2.3	4.0

      An exemplary embodiment of the present disclosure includes a method of producing high-quality liquid fuels that includes mixing a solid plastic waste with a metal hydride and a supported metal catalyst; gasifying the mixture; and producing the high-quality liquid fuels.

      An exemplary embodiment of the present disclosure includes a method of producing high-quality liquid fuels that includes melting a solid plastic waste; adding a metal hydride and a supported metal catalyst; and producing the high-quality liquid fuel.

      An exemplary embodiment of the present disclosure includes a high-quality fuel prepared by a process that includes mixing a solid plastic waste