Abstract: The invention objective a Individual Bagasse Drier that realizes a system of utilization of the chimney gases, to decrease the moisture of the bagasse left from the mill in 10 or 15 points, increasing the steam production between 13.5% to 15.45% respectively.It consists of a drier for each furnace, and consumes 54% of the power installed per ton of dry bagasse, in relation to the existing systems in the market.

Abstract: Overall heat recovery from wet wood waste, particularly sawmill-generated hog fuel, is improved by a process for predrying the fuel. A wet oversize fraction of the fuel is combusted in a fluid bed reactor providing heat for drying the remaining smaller sized fraction of the waste pile to about 10-30% moisture by weight. The gaseous products of the fluid bed burning are contacted with the fuel fraction in, preferably, a rotary dryer. The dried fuel is then screened into coarse and fine fractions. The coarse fraction is fed onto a grate of a wood waste boiler. The fines fraction is injected into the boiler combustion in an air suspension. The amount of fuel fed to the fluid bed reactor is 10-25% of the total fuel flow, depending upon the moisture content of the fuel. The gases fed to the rotary dryer are less than about 1,200.degree. F., to minimize "blue haze," by combining with minimum outside air.

Abstract: A coal feed system for use in a fluidized bed in which a grate is supported in a housing and is adapted to receive, on its upper surface, a bed of particulate material including a combustible fuel. Air is passed through the grate and into the bed to fluidize the particulate material. The particulate fuel material is separated externally of the bed into a relatively coarse material which is distributed over the upper surface of the bed and a relatively fine material which is distributed into the bed below the upper surface.

Abstract: Solid particles comprising combustible matter (e.g. coal) associated with or contaminated by inert matter (e.g. ash, rock) is segregated in a segregation zone into low density/small size and high density/large size fractions. The low density/small size fractions are passed to a utilization zone for conversion of the combustible matter. The high density/large size fractions are size reduced (e.g. by grinding) and either returned to the segregation zone, or passed at least in part, directly to the utilization zone. The conversion of the combustion matter proceeds more efficiently as a result. The segregation zone may operate by fluidized size/density segregation and in the utilization zone, the combustible matter may be at least partially combusted, preferably in a fluidized bed.

Abstract: Any bundles in household refuse are broken up and this refuse is then coarsely comminuted with the broken up bundles, only the hard components of the refuse being comminuted with the light components merely being temporarily deformed between a pair of rollers having surface formations. Thereafter the coarsely comminuted refuse is separated by means of a drum-type sieve into a heavy fraction and a light fraction. The light fraction is finely comminuted into granules which are blown into a burning chamber in which they are suspended on a gas. The granules are combusted in this chamber to form a hot gas that is recirculated to sterilize and dry the heavy fraction and to dry the finely comminuted light fraction before its burning.