Nonindustrial straw pellets should comply with limitations
on the
content of ash, chlorine, nitrogen, sulfur, and heavy metals, and
have a high melting temperature of ash. To produce such pellets, the
properties of straw can be improved by leaching. In known papers,
the completion of chlorine washing-out was not controlled. Aims of
the paper were to study ash solubility at leaching of straw until
completion of chlorine removal and to make a conclusion on studied
straw suitability for the production of nonindustrial pellets. Aims
were achieved by straw soaking with heating to 100 °C and subsequent
plug flow flashing with control of leaching completion by the absence
of chlorine in leachate; studying the ash, chlorine, nitrogen, sulfur,
and heavy metals content of straw; studying the thermal behavior of
ash at heating; determining the initial deformation temperature (IDT)
of ash; and comparing the properties of original and leached straw
with the specification of straw pellets. Straw leaching until completion
of chlorine washing-out provided decreasing chlorine, nitrogen, and
sulfur contents below limitations, and the ash content decreased from
7.15 to 3.93% at water leaching to 4.29% at leaching with a 10% solution
of acetic acid. In the ternary diagram, the composition of straw ash
shifted from a zone of low melting eutectics to zones of high-melting
tridymite and cristobalite. The IDT of the original straw ash was
847, 1250 °C after water leaching, and above 1275 °C after
leaching with an acetic acid solution. Monitoring the absence of chlorine
in the leaching liquid can be applied as a control parameter for straw
leaching completion. The original straw was not suitable for the production
of nonindustrial pellets because of the high contents of Cl, S, and
Cr and the low IDT of ash. All indexes of straw were improved due
to leaching, but the Cr content was above limitation. Producers of
pellets need to assess straw suitability as to heavy metal content
both in the original and leached states.