首页> 外国专利> Binderless briquetting of hard brown coal, bituminous coal and similar coals comprises processing raw coal, drying raw coal, treating dry coal, briquetting and treating briquette

Binderless briquetting of hard brown coal, bituminous coal and similar coals comprises processing raw coal, drying raw coal, treating dry coal, briquetting and treating briquette

机译:硬褐煤,烟煤和类似煤的无粘结剂压块包括加工原煤,干燥原煤,处理干煤,压块和压块

摘要

Binderless briquetting of hard brown coal, bituminous coal and similar coals comprises: (a) processing raw coal; (b) drying raw coal; (c) treating dry coal; (d) briquetting; and (e) treating briquette. The raw coal is initially screened to a particle size of = 6.3 mm and present oversized particles are crushed in a hammer mill (3). The crushed raw coal is dried in a steam-heated tube dryer (6) for soft brown coal to a final water content of 9-11 mass% with the use of hard brown coal and 1-3 mass% with the use of bituminous coal. Binderless briquetting of hard brown coal, bituminous coal and similar coals comprises: (a) processing raw coal; (b) drying raw coal; (c) treating dry coal; (d) briquetting; and (e) treating briquette. The raw coal is initially screened to a particle size of = 6.3 mm and present oversized particles are crushed in a hammer mill (3). The crushed raw coal is dried in a steam-heated tube dryer (6) for soft brown coal to a final water content of 9-11 mass% with the use of hard brown coal and 1-3 mass% with the use of bituminous coal, where the tube dryers relative to a known tube dryers for soft brown coal and apparatus is modified technologically. The dried and tempered coal is further crushed to an optimum particle size of = 0.5 mm in the tube dryers at 70-90[deg] C for briquetting by means of a steam-heated reservable impact hammer mill in collaboration with a suitable sifter, where the dry coal and oversized particles are added for treating the briquette. The briquetting of the processed dry coal is carried out by a two-roll press (18) exhibiting: a particle size of the dry coal of = 0.5 mm; water content of the dry coal of 9-11mass% with hard brown coal and 1-3 mass% with bituminous coal; temperature of the dry coal at 70-90[deg] C; pressure of 140-180 MPa; specific pressing force of 150 kN/cm; and pressing material vaporization prior to the pressing, where a scabs band is formed by an scabs crusher, which is designed as two-roll crusher, are divided into individual briquettes. The scabs break and the trickle coal from the two-roll press are sieved from the individual briquettes as an end product of the method and the dry coal is mixed in the region of the treating dry coal. An independent claim is also included for a plant for binderless briquetting of hard brown coal, bituminous coal and similar coals, where a bunker (1) with overlapping raw coal with a maximum particle size of 60 mm is connected downstream to a sifter (2) for separating the passage particle with a particle size of = 6.3 mm from the oversized particle and the hammer mill is installed for crushing the oversized particles to = 6.3 mm. A bunker is provided for temporary storage of the crushed raw coal with a particle size of = 6.3 mm. The bunker is connected downstream to the steam-heated tube dryer for drying the processed raw coal to the final water content of 9-11 mass% with the use from hard brown coal and 1-3mass% with the use of bituminous coal, and the tube dryer is associated with an electrostatic precipitator for the disposal of the resulting vapor and for returning the separated dry coal dust in the method. The drying is followed by the region for treating dry coal comprising the steam-heated reservable impact hammer mill with upstream- and downstream rotary valves, where the treated dry coal leaves the impact hammer mill with the particle size of = 0.5 mm. The impact hammer mill is connected downstream to a vibrating channel and one sifter in the form of a multiple-deck or a sizer for separating the oversized particles (greater than 0.5 mm) from the desired particles (less than 0.5 mm), where a bunker is provided for storage of the desired particles and a transporting device is provided for the reintroduction of oversized particles in the method. The at least warm dry coal at 70[deg] C after pressing is realized to scabs band by the two-roll press with pressing material vaporization prior to the pressing. The scabs crusher is formed as the two-roll crusher provided for breaking the scabs band into individual briquettes. The scabs crusher is followed by a further sifter for separating resulting fine particle from the individual briquettes during the pressing and crushing, where the fine particle in the region for treating dry coal is introduced back into the method.
机译:硬褐煤,烟煤和类似煤的无粘结剂团块包括:(a)加工原煤; (b)干燥原煤; (c)处理干煤; (d)压块; (e)处理煤饼。首先将原煤筛分至= 6.3 mm的粒度,然后将当前的超大颗粒在锤磨机(3)中破碎。压碎的原煤在蒸汽加热的管式干燥机(6)中进行干燥,使用硬褐煤将软褐煤干燥至最终水含量为9-11质量%,而使用烟煤则达到1-3质量% 。硬褐煤,烟煤和类似煤的无粘结剂团块包括:(a)加工原煤; (b)干燥原煤; (c)处理干煤; (d)压块; (e)处理煤饼。首先将原煤筛分至= 6.3 mm的粒度,然后将当前的超大颗粒在锤磨机(3)中破碎。压碎的原煤在蒸汽加热的管式干燥机(6)中进行干燥,使用硬褐煤将软褐煤干燥至最终水含量为9-11质量%,而使用烟煤则达到1-3质量% ,其中管式干燥机相对于已知的用于软褐煤和设备的管式干燥机进行了技术改造。在70-90℃的管式干燥机中,将经过干燥和回火的煤进一步破碎至最佳粒径= 0.5 mm,以便通过蒸汽加热的可蓄能冲击锤式破碎机与合适的筛分机一起进行压块。加入干煤和超大颗粒来处理团块。经处理的干煤的团块通过两辊压机(18)进行,该压机表现出:干煤的粒度为0.5mm;干煤与硬褐煤的含水量为9-11质量%,烟煤为1-3质量%;干煤的温度为70-90℃;压力为140-180 MPa; 150 kN / cm的比压力;在压制之前,压制材料汽化,其中由构造为两辊式压碎机的sc子破碎机形成a子带,将其分成单个团块。从该方法的最终产品中,将break渣破裂和来自两辊压榨机的滴流煤从各个团块中过筛,然后在处理过的干煤区域中混合干煤。还包括针对硬褐煤,烟煤和类似煤的无粘结剂团块化的工厂的独立权利要求,其中具有最大粒度为60毫米的重叠原煤的料仓(1)在下游连接到筛分机(2)为了从过大的颗粒中分离出粒径为= 6.3mm的通道颗粒,并安装了锤磨机以将过大的颗粒粉碎至= 6.3mm。提供了一个沙坑,用于临时存储粒度为6.3毫米的碎煤。料仓的下游连接到蒸汽加热管式干燥机,用于将处理后的原煤干燥,最终水含量为9-11质量%(使用硬褐煤),1-3质量%(使用烟煤),管式干燥机与静电除尘器相连,用于处理所产生的蒸气并在该方法中返回分离出的干燥煤粉。干燥之后是干燥煤的处理区域,该区域包括带有上游和下游旋转阀的蒸汽加热的可储式冲击锤式粉碎机,其中处理过的干燥煤以= 0.5 mm的粒径离开冲击锤式粉碎机。冲击锤式粉碎机在下游连接到振动通道和一个筛子,该筛子为多层或分级筛的形式,用于将超大颗粒(大于0.5毫米)与所需颗粒(小于0.5毫米)分离,并在一个仓中在该方法中,提供了用于存储所需颗粒的容器和提供了用于将超大颗粒重新引入的运输装置。通过双辊压机在压制之前使压制材料汽化,从而在压制之后在70℃下至少温热的干燥煤实现结to带。 sc结石破碎机形成为两辊破碎机,其被设置用于将ab结石带破碎成单独的团块。 ab渣破碎机之后是另一台筛分机,用于在压榨和破碎过程中从单个团块中分离出所得的细颗粒,其中将用于处理干煤的区域中的细颗粒引入该方法中。

著录项

  • 公开/公告号DE102010053593A1

    专利类型

  • 公开/公告日2012-06-14

    原文格式PDF

  • 申请/专利权人 ZEMAG MASCHINENBAU GMBH;

    申请/专利号DE20101053593

  • 发明设计人 MINYAN FU;STEIDL RUDOLF;

    申请日2010-12-07

  • 分类号C10L5/08;

  • 国家 DE

  • 入库时间 2022-08-21 17:05:13

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