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METHOD FOR DRYING BULK CARBON OR MINERAL MATERIALS AND INSTALLATION FOR DRYING BULK CARBON OR MINERAL MATERIALS (OPTIONS)

机译:散装碳或矿物材料的干燥方法和散装碳或矿物材料的干燥安装(选装)

摘要

FIELD: heating.;SUBSTANCE: drying method of granular carbonaceous or mineral materials with humidity providing granular state of material involves heat supply on several levels from heat carrier to material mass. Immediately above each level of heat supply from heat carrier there performed is heat carrier and/or steam removal; distance between level of heat supply from heat carrier and heat carrier and/or steam removal level located immediately above it, as well as between heat carrier and/or steam removal level and level of heat supply from heat carrier, which is located immediately above it, comprises at least six times maximum size of material particle; heat carrier velocity is at least 0.1 m/s; heat carrier temperature is at least 130°C; heat from heat carrier is injected into mass continuously moving in downward direction. As per the first version of the method's implementation, the drying plant of granular carbonaceous or mineral materials includes a chamber intended to supply granular material to it; in the chamber cavity there are elements for injection of heat carrier to the chamber and element of heat carrier removal from the chamber; besides, each heat carrier supply and removal element is made in the form of a channel passing through the chamber cavity and interconnected with the chamber inner cavity; each channel intended for heat carrier injection is interconnected with the heat carrier source; the plant includes at least two tiers of heat carrier injection and removal. Each tier includes heat carrier injection channels made on one level and heat carrier removal channels made on one level too, which are located immediately above heat carrier injection channel level at some distance from them. Distance between level of heat carrier injection/removal channels and level of heat carrier removal/injection channels, which is located immediately above it, is at least six times maximum size of material particle; also, distance between adjacent channels located on one and the same level is at least six times maximum size of material particle; heat carrier source is intended for supply of heat carrier gas to the chamber. As per the second version of the method's implementation, the drying plant of granular carbonaceous or mineral materials includes a chamber designed for supply to it of granular material; in the chamber cavity there are elements for injection of heat carrier heat to the chamber and elements for removal of steam from the chamber, which is formed at material drying. Each element for injection of heat carrier heat is made in the form of a closed channel passing through the chamber cavity and interconnected with the heat carrier source and with other channels for injection of heat carrier heat; each steam removal element is made in the form of a channel passing through the chamber cavity and interconnected with the chamber inner cavity; each channel intended for injection of heat carrier heat is interconnected with the heat carrier source; the plant includes at least two tiers of channels for injection of heat carrier heat and removal of steam; besides, each tier includes heat carrier heat injection channels made on one level and steam removal channels made on the same level too and located immediately above level of channels for heat carrier heat injection at some distance from them. Distance between level of heat injection channels from heat carrier and level of steam removal channels, which is located immediately above it, is at least six times maximum size of material particle; also, distance between level of steam removal channels and level of heat injection channels from heat carrier, which is located immediately above it, is at least six times maximum size of material particle; heat carrier is intended for supply of heat carrier gas to the chamber.;EFFECT: simpler design of the drying plant of granular materials; improved drying efficiency.;18 cl, 12 dwg
机译:领域:加热;物质:具有湿度的颗粒状含碳或矿物材料的干燥方法提供了材料的颗粒状态,涉及从热载体到材料块的多个级别的热供应。在热载体的每个供热水平之上立即执行热载体和/或蒸汽的去除;载热体和/或载热体的供热水平和/或紧接在其上方的蒸汽去除水平之间的距离,以及载热体和/或蒸汽除去水平与紧靠其上方的载热体的供热水平之间的距离,其至少是材料颗粒最大尺寸的六倍;载热体速度至少为0.1 m / s;载热体温度至少为130°C;来自热载体的热量被注入到连续向下移动的物质中。根据该方法实施的第一个版本,粒状碳质或矿物材料的干燥设备包括一个旨在向其供应粒状材料的腔室;在腔室腔中,具有用于将热载体注入腔室的元件以及从腔室中去除热载体的元件。另外,各载热体的供排体形成为通道,该通道穿过腔室并与腔室内腔相互连接。用于热载体注入的每个通道与热载体源互连。该工厂至少包括两层热载体注入和移除层。每一层包括在一个水平上制成的载热体注入通道和也在一个水平上制成的载热体去除通道,它们位于载热体注入通道水平的正上方,与它们相距一定距离。热载体注入/去除通道的高度与紧邻其上方的热载体去除/注入通道的高度之间的距离至少是材料颗粒最大尺寸的六倍;同样,位于同一水平面上的相邻通道之间的距离至少是材料颗粒最大尺寸的六倍;热载体源旨在向腔室供应热载体气体。根据该方法实施的第二种形式,粒状碳质或矿物材料的干燥设备包括一个设计用于向其供应粒状材料的腔室。在腔室腔中,具有用于将热载体热注入腔室的元件以及用于从腔室去除蒸汽的元件,其在材料干燥时形成。每个用于注入载热的元件均制成封闭通道的形式,该封闭通道穿过腔室并与载热源以及与其他用于注入载热的通道互连。每个蒸汽去除元件以通道的形式制成,该通道穿过腔室腔并与腔内部腔互连。用于注入载热体热量的每个通道都与载热体源互连。该设备至少包括两层通道,用于注入热载体热量和去除蒸汽。此外,每一层还包括在同一层上形成的载热体注热通道和在同一层上形成的蒸汽去除通道,这些蒸汽去除通道位于与载热体注入通道相距一定距离的通道的正上方。位于热载体上方的注热通道的高度与紧邻其上方的蒸汽排出通道的高度之间的距离,至少是材料颗粒最大尺寸的六倍;同样,排汽通道的高度与热载体的热注入通道之间的距离(直接位于其上方)至少是材料颗粒最大尺寸的六倍;热载体用于向腔室供应热载体气体。效果:颗粒状物料干燥设备的设计更简单;干燥效率更高;; 18 cl,12 dwg

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