Pyrolysis of hydrolytic
lignin (HL) in newly designed, gas phase
continuous droplet evaporation (CDE) and continuous atomization (CA)
reactors was studied. The product distribution was strongly dependent
on the heterogeneous character of either delivery of lignin solution
into the CDE reactor (in situ formation of solid phase) or sampling
conditions using quartz wool in both CDE and CA reactors. The effect
of residence time, initial concentration of HL solution, and injection
temperature on product distribution in the CDE reactor was investigated
and discussed in terms of mass and heat transfer limitation. The experimental
data confirm that at low initial mass delivery rates of lignin (micrograms
per second) and by increasing initial lignin concentration (up to
40 times), the formation of phenolics is slightly intensified (six
times). However, the solid surface or any condensed phase that forms
in situ during the reaction in the gas phase may largely govern the
pyrolysis processes. The detailed experimental examination of homogeneous
pyrolysis of lignin in both gas-phase reactors by implication of diverse
analytical techniques (gas chromatography, gel permeation chromatography,
laser desorption/ionization, Fourier transform infrared spectroscopy,
electron paramagnetic resonance, nuclear magnetic resonance ) revealed
break down of HL macromolecules into oligomer fragments after pyrolysis
at negligible amounts of phenolics detected. A mechanistic interpretation
of primary steps for formation of dominant intermediate products,
oligomers and oligomer stable radicals, is represented.