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Pyrolysis of cyclohexanone-formaldehyde resins at 650 C for 5 s showing differences due to source and ageing. Identified peaks are

Pyrolysis of Cyclophanes

Pyrolysis of different molecular mass

Pyrolysis of Distillation Bitumen and its Colloidal Components in 10 bar Methane Half Life Time ty 2 versus Temperature Line 1

Pyrolysis of Distillation Bitumen in 1 bar Argon Half Life Time versus Temperature

Pyrolysis of Heavy Residues

Pyrolysis of in a nitrogen atmosphere .

Pyrolysis of isobutane in the presence of HCl or HBr. Variations of the relative magnitude of the two stoichiometries vs. initial concentration of additive YH.

Pyrolysis of isobutane. High total selectivi-ties at low pressures can be had.

Pyrolysis of isobutane. Isobutylene selectivity decreases with conversion and pressure.

Pyrolysis of isobutane. Propylene selectivity is almost constant at atmospheric pressure.

Pyrolysis of isopentane 25 mmHg , at

Pyrolysis of isopentane in a batch reactor. T 480 C, 25 mmHg,

Pyrolysis of kerogens at a standard heating rate of 4 C min 1 up to various final temperatures. Mass balance is of recovered and nonrecovered products plus

Pyrolysis of kuwanon G octamethyi ether

Pyrolysis of LDPE

Pyrolysis of lumped component of branched alkanes C15H32. Selectivity of methyl radical and small alkenes as a function of the probability of methyl substitution.

Pyrolysis of methyl-2-butenyIphosphonate.

Pyrolysis of neopentane in a batch reactor

Pyrolysis of neopentane in a batch reactor reaction order at conversion equal to zero.

Pyrolysis of neopentane in a batch reactor the Arrhenius law.

Pyrolysis of neopentane inhibited by added isobutene

Pyrolysis of neopentane with added isobutene and oxygen. o and r variable.

Pyrolysis of neopentane with small amounts of oxygen o 2, 3

Pyrolysis of one-sided non benzylic disulfones



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