首页> 外文会议>Proceedings of the 20th international conference on fluidized bed combustion(FBC) >INTEGRATED USE OF FLUIDIZED BED TECHNOLOGY FOR OIL PRODUCTION FROM OIL SHALE
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INTEGRATED USE OF FLUIDIZED BED TECHNOLOGY FOR OIL PRODUCTION FROM OIL SHALE

机译:综合利用流化床技术从油页岩中采油

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The plant unit which consists of a fluidized bed retort and CFB furnace for burning the by-products of retorting (semicoke and semicoke gas) is presented in this paper. The oil shale retort consists of a fast fluidized bed shaft, coarse semicoke bit, semicoke separation chamber and cyclone for the separation of fine semicoke particles. The crashed oil shale and hot ash from the CFB ash separator are fed concurrently into the fast fluidized bed shaft. For fluidizing the mixture of oil shale and hot ash particles, the recycle semicoke gas is used. The pyrolysis of oil shale begins in fluidized bed and is completed in the semicoke separation chamber. The coarse semicoke particles are separated from fluidized bed directly while the medium size particles are separated from the gases in the semicoke separation chamber and the finest semicoke particles in the cyclone. All the fractions of semicoke from the fluidized bed retort and semicoke gas from the oil fractionator are burnt in the CFB furnace. The semicoke ash is separated from flue gases in the CFB ash separator. A part of separated hot ash is fed into the fluidized bed retort as a solid heat carrier material and the rest into the furnace through the ash cooler or separated from the process. The retention of sulphur dioxide formed during the semicoke and semicoke gas combustion, is guaranteed for about 99% due to the high CaO content in the semicoke ash and convenient temperature (about 850℃) in the CFB furnace. The described plant unit is useful for retorting oil shale and other solid hydrocarbon-containing fuels. The advantages of the present retorting process and system are: improved oil yield, greater throughput, lower retorting time, avoidance of moving parts in the retorting zones, reduced downtime, etc. A new plant unit for oil shale oil production has been elaborated and defended by the Estonian Utility Model EE 2007 00671 U1.
机译:本文介绍了由流化床蒸馏器和CFB炉组成的装置单元,用于燃烧蒸馏的副产物(半焦和半焦气)。油页岩干馏塔由快速流化床竖井,粗半焦钻头,半焦分离室和用于分离细半焦颗粒的旋风分离器组成。来自CFB灰分分离器的油页岩和热灰分同时进入快速流化床竖井。为了使油页岩和热灰烬颗粒的混合物流化,使用了再循环的半焦气。油页岩的热解始于流化床,并在半焦分离室中完成。将粗的半焦颗粒直接从流化床中分离出来,而将中型颗粒从半焦分离室中的气体和旋风分离器中最细的半焦颗粒中分离出来。流化床蒸馏器产生的所有半焦馏分和油分离器产生的所有半焦气均在CFB炉中燃烧。在CFB灰分离器中将半焦灰与烟气分离。一部分分离出的热灰作为固体载热材料被送入流化床蒸馏器,其余部分则通过灰冷却器或与工艺分离。半焦和半焦气体燃烧过程中形成的二氧化硫的保留量可保证达到约99%,这是因为半焦灰中的CaO含量较高,并且CFB炉的温度较高(约850℃)。所描述的工厂单元可用于蒸馏油页岩和其他含固体烃的燃料。目前的蒸馏工艺和系统的优点是:提高了油产量,提高了产量,缩短了蒸馏时间,避免了在蒸馏区中移动部件,减少了停机时间等。精心设计并捍卫了新的油页岩油生产装置由爱沙尼亚实用新型EE 2007 00671 U1提供。

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