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Fluidized-bed co--gasification of residual biomass/poor coal blends for fuel gas production

机译:残余生物质/贫煤混合物流化床共气化生产燃气

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Experiments involving the co-gasification of residual biomass/poor coal blends and gasification of individual feedstocks used in the blends were performed in a bench scale, continuous fluidized-bed working at atmospheric pressure. Two types of blends were prepared, mixing pine chips (from Valcabadillo, Spain) with black coal, a low-grade coal from Escatron, Spain, and Sabero coal, a refuse coal from Sabero, Spain, in the ratio range of 0/l00-- l00/0. Experimental tests were can.ied out using as a gasification agent mixtures of air and steam with dew points of 74--85deg.C at gasification temperatures of 840--9l0deg.C and superficial fluidized gas velocities of 0.7-- l.4 m/s. Feasibility studies were very positive, showing that blending effectively improved the performance of fiuidized-bed co-gasification of the low-grade coal, and the possibility of converting the refuse coal to a low-Btu fuel gas. This study indicates that a blend ratio with no less than 20/100 pine chips for the low--grade coal and 40/100 pine chips for the refuse coal are the most appropriate. The dry product gas low heating value augments with increasing blend ratio from 3700 to 4560 kJ/N m~3 for pine chips/low-grade coal, and from 4000 to 4750 kJ/N m~3 for pine chips/refuse coal. Dry product gas yield rises with the increase of the blend ratio from l.80 to 3.20 N m~3/kg (pine chips/low-grade coal), and from 0.75 to l.75 N m~3/kg (pine chips/refuse coal), respectively. About 50/100 co-gasification process overall thermal efficiency can be achieved for the two types of blend.
机译:在工作台规模,连续流化床,大气压下进行的实验涉及剩余生物质/贫煤混合物的共气化和混合物中使用的各种原料的气化。制备了两种类型的混合物,将松木屑(来自西班牙Valcabadillo的煤)与黑煤(来自西班牙Escatron的低级煤)和Sabero煤(来自西班牙Sabero的垃圾煤)以0 / l00的比例进行混合。 -100/0。可以使用露点为74--85°C的空气和蒸汽的混合物在840--9l0°C的气化温度和0.7--1.4 m的表观流化气体速度下作为气化剂进行实验测试/ s。可行性研究非常积极,表明掺混有效地改善了低品位煤的流化床共气化性能,并有可能将垃圾煤转化为低Btu燃气。这项研究表明,低品位煤的混合比不少于20/100松木屑,垃圾煤的混合比不少于40/100松木屑是最合适的。干品气的低热值随着松木/低品位煤的混合比从3700增加到4560 kJ / N m〜3,松木/废煤从4000增加到4750 kJ / N m〜3。干品气产量随混合比从1.80 N m〜3 / kg(松木片/低品位煤)增加到从1.80 N m〜3 / kg(松木片/低级煤)到0.75至1.75 N m〜3 / kg(松木片) /拒绝煤)。两种混合物的共气化工艺总热效率约为50/100。

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