SUPPLY OF RAW MEAL VIA SCOOP CHAMBER

1508840 Preheating granular material F L SMIDTH & CO AS 3 Sept 1976 [15 Oct 1975 19 Nov 1975 4 Feb 1976] 42221/75 47632/75 and 4362/76 Heading F4B In a kiln plant comprising a multistage preheater and a rotary kiln, material from a preheater stage other than the last is fed to a dispersing devic...

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description 1508840 Preheating granular material F L SMIDTH & CO AS 3 Sept 1976 [15 Oct 1975 19 Nov 1975 4 Feb 1976] 42221/75 47632/75 and 4362/76 Heading F4B In a kiln plant comprising a multistage preheater and a rotary kiln, material from a preheater stage other than the last is fed to a dispersing device mounted on the upper end of the kiln, and material from the last preheater stage is fed to the kiln beyond the dispersing device. In one embodiment, Figs. 3 and 6, a duct 4 leads preheated material into the kiln end, and a duct 5 leads material from the penultimate preheater to a scoop chamber 3 having lifters 9 scattering material into the gas flow, and air inlets 17 allowing the entry of cooling air. The supply duct 4 is located below the sloping floor 2a of the smoke box 2 leading to the preheaters thus reducing the cross-section and accelerating the gas flow. A by-pass pipe 16 for kiln gases may be provided. In another embodiment (Figs. 7 and 8) the upper end of the kiln carries scoops on its outer surface, a stationary chamber surrounding the kiln end receiving material from the penultimate preheater stage. The dispersing device may take the form of stationary plates 27a at the entry of the smoke box 2, Fig. 9. The Specification shows various arrangements of cyclone preheaters, coolers and calciners similar to those shown in Specifications 1,469,673 and 1,479,220. Specifications 763,837, 1,100,530, 1,375,566 and 1,453 215 are referred to.
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In one embodiment, Figs. 3 and 6, a duct 4 leads preheated material into the kiln end, and a duct 5 leads material from the penultimate preheater to a scoop chamber 3 having lifters 9 scattering material into the gas flow, and air inlets 17 allowing the entry of cooling air. The supply duct 4 is located below the sloping floor 2a of the smoke box 2 leading to the preheaters thus reducing the cross-section and accelerating the gas flow. A by-pass pipe 16 for kiln gases may be provided. In another embodiment (Figs. 7 and 8) the upper end of the kiln carries scoops on its outer surface, a stationary chamber surrounding the kiln end receiving material from the penultimate preheater stage. The dispersing device may take the form of stationary plates 27a at the entry of the smoke box 2, Fig. 9. The Specification shows various arrangements of cyclone preheaters, coolers and calciners similar to those shown in Specifications 1,469,673 and 1,479,220. 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In one embodiment, Figs. 3 and 6, a duct 4 leads preheated material into the kiln end, and a duct 5 leads material from the penultimate preheater to a scoop chamber 3 having lifters 9 scattering material into the gas flow, and air inlets 17 allowing the entry of cooling air. The supply duct 4 is located below the sloping floor 2a of the smoke box 2 leading to the preheaters thus reducing the cross-section and accelerating the gas flow. A by-pass pipe 16 for kiln gases may be provided. In another embodiment (Figs. 7 and 8) the upper end of the kiln carries scoops on its outer surface, a stationary chamber surrounding the kiln end receiving material from the penultimate preheater stage. The dispersing device may take the form of stationary plates 27a at the entry of the smoke box 2, Fig. 9. The Specification shows various arrangements of cyclone preheaters, coolers and calciners similar to those shown in Specifications 1,469,673 and 1,479,220. 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In one embodiment, Figs. 3 and 6, a duct 4 leads preheated material into the kiln end, and a duct 5 leads material from the penultimate preheater to a scoop chamber 3 having lifters 9 scattering material into the gas flow, and air inlets 17 allowing the entry of cooling air. The supply duct 4 is located below the sloping floor 2a of the smoke box 2 leading to the preheaters thus reducing the cross-section and accelerating the gas flow. A by-pass pipe 16 for kiln gases may be provided. In another embodiment (Figs. 7 and 8) the upper end of the kiln carries scoops on its outer surface, a stationary chamber surrounding the kiln end receiving material from the penultimate preheater stage. The dispersing device may take the form of stationary plates 27a at the entry of the smoke box 2, Fig. 9. The Specification shows various arrangements of cyclone preheaters, coolers and calciners similar to those shown in Specifications 1,469,673 and 1,479,220. Specifications 763,837, 1,100,530, 1,375,566 and 1,453 215 are referred to.</abstract><oa>free_for_read</oa></addata></record>
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subjects ARTIFICIAL STONE
BLASTING
CEMENTS
CERAMICS
CHEMISTRY
COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDINGMATERIALS
CONCRETE
DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS,IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KINDOF FURNACE
FERROUS OR NON-FERROUS ALLOYS
FURNACES
FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL
HEATING
KILNS
LIGHTING
LIME, MAGNESIA
MECHANICAL ENGINEERING
METALLURGY
OPEN SINTERING OR LIKE APPARATUS
OVENS
PRETREATMENT OF RAW MATERIALS
PRODUCTION AND REFINING OF METALS
REFRACTORIES
RETORTS
SLAG
TREATMENT OF ALLOYS OR NON-FERROUS METALS
TREATMENT OF NATURAL STONE
WEAPONS
title SUPPLY OF RAW MEAL VIA SCOOP CHAMBER
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