Highly dense red mud shields for x-ray and gamma-ray attenuation
US-2024018050-A1 · Jan 18, 2024 · US
US9776922B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9776922-B2 |
| Application number | US-201314022619-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 10, 2013 |
| Priority date | Mar 17, 2011 |
| Publication date | Oct 3, 2017 |
| Grant date | Oct 3, 2017 |
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Official abstract text for this publication.
The invention provides a shuttle kiln that can fire ceramic porous bodies containing organic binders in a shorter period of time than in conventional methods without occurring breaks due to a temperature difference between the inside and the outside. The shuttle kiln of the invention is suited for firing of ceramic porous bodies containing organic binders. It includes a gas suction path 4 that suctions in-furnace gas and discharges it via an afterburner 5 and a circulation path 7 that suctions the in-furnace gas to the furnace outside to burn organic binder gas and then returns it into the furnace.
Opening claim text (preview).
The invention claimed is: 1. A shuttle kiln for firing ceramic porous bodies containing organic binders, the kiln comprising: a gas suction path that includes at least one gas suction port for suctioning an in-kiln gas outside the kiln and exhausting the in-kiln gas to the atmosphere via an afterburner; and a circulation path for suctioning the in-kiln gas outside the kiln, burning an organic binder gas contained in the in-kiln gas, and then recirculating the in-kiln gas back into the kiln, wherein the gas suction path and the circulation path are completely independent of each other, wherein the ceramic porous bodies are loaded on a carriage that reciprocates between the inside and the outside of the kiln, wherein the gas suction path and the gas suction port are located at a lower part of the carriage, and wherein the circulation path includes a catalytic reactor vessel for catalytic combustion of the suctioned in-kiln gas. 2. The shuttle kiln according to claim 1 , wherein the in-kiln gas is suctioned to the circulation path from a side wall of the kiln body. 3. The shuttle kiln according to claim 1 , further comprising a fuel gas supply pipe mounted in the circulation path upstream of the catalytic reactor vessel and used to supply a fuel gas. 4. The shuttle kiln according to claim 1 , wherein the circulation path comprises: a heating device mounted upstream of the catalytic reactor vessel and used to heat the suctioned in-kiln gas; and a cooling device mounted downstream of the catalytic reactor vessel and used to lower a temperature of the gas having passed through the catalytic reactor vessel to a predetermined temperature. 5. The shuttle kiln according to claim 3 , wherein the circulation path comprises: a heating device mounted upstream of the catalytic reactor vessel and used to heat the suctioned in-kiln gas; and a cooling device mounted downstream of the catalytic reactor vessel and used to lower a temperature of the gas having passed through the catalytic reactor vessel to a predetermined temperature.
Processes characterised by the flow of gas · CPC title
Burning or sintering processes (C04B33/32 takes precedence {; powder metallurgy B22F}) · CPC title
Heating rate · CPC title
Forming or maintaining special atmospheres or vacuum within heating chambers (supplying steam, vapour, gases or liquids F27D7/02) · CPC title
at an oxygen percentage below that of air · CPC title
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