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    • 5. 发明授权
    • Method for drying coal and cooling coke
    • 干燥煤和冷却焦炭的方法
    • US4470878A
    • 1984-09-11
    • US468301
    • 1983-02-22
    • Vladan PetrovicKarl SchmidFriedrich JokischHeinz Rotthaus
    • Vladan PetrovicKarl SchmidFriedrich JokischHeinz Rotthaus
    • C10B39/02C10B57/10C10L9/08
    • C10B39/02C10B57/10Y10S165/92
    • In a coking process, coal to be coked is preheated in a cascaded whirling bed drier into which the coal is charged from above and exposed to an indirect heat transfer while whirling in a coal-stream mixture. Hot gas applied to the heating pipes in respective cascades of the drier is branched off from the total amount of hot gases discharged from a dry cooler in which hot coke from the coke oven is cooled by recirculating cooler gas constituted by a partial gas stream discharged from the cascades of the drier and reunited with the other partial stream subject to a heat exchange for generating steam. Steam from the whirling beds is discharged from the cascaded drier, separated from the entrained dust particles, and then the excessive steam is drained in a branch conduit and the remaining steam is compressed and reintroduced into the lowermost whirling bed in the drier.
    • 在焦化过程中,待焦化的煤在级联的旋转床式干燥器中预热,煤从上方进料,并在煤流混合物中旋转时暴露于间接热传递。 施加到干燥器各个级联中的加热管的热气体从干燥冷却器排出的热气体总量中分支出来,其中焦炉的热焦由通过从由焦炉排出的部分气流构成的再循环冷却气体冷却 干燥器的级联并与另一部分流重合,进行热交换以产生蒸汽。 来自旋转床的蒸汽从级联的干燥器中排出,与夹带的灰尘颗粒分离,然后在分支导管中排出过量的蒸汽,并将剩余的蒸汽压缩并再次引入干燥器中的最低旋转床。