Development of fluidized-bed cement calcination process with energy conservation and low pollutant generatic
Development of fluidized-bed cement calcination process with energy conservation and low pollutant generatic
批准号:
06558066
负责人:
YOSHIDA Kunio
金额:
$10.24万
依托单位:
依托单位国家:
日本
项目类别:
Grant-in-Aid for Scientific Research (A)
财政年份:
1994
资助国家:
日本
项目状态:
已结题
起止时间:
1994 至 1997
中文摘要
研究结果分为两个主题:(1)阐明喷流床中固体循环机理;(2)开发流化床水泥生产工艺的放大方法。(1)带导流管的喷流床内颗粒循环特性所提出的流化水泥生产工艺由两级流化床组成。:一为上喷床造粒,一为下流化床煅烧。为了在1300℃的温度下完成煅烧而不产生结块问题,必须在上部喷床上产生均匀的颗粒。在此基础上,采用直径为0.205m、带导流管的喷流床研究了气速对固体循环行为的影响。通过内窥镜目视观察、压力波动和光信号分析,发现固体颗粒周期性地从环空进入气体射流,并在尾水管中向上移动。然而,在一定的最大气速下,固体流动变得均匀,向上输送而不形成团簇。(2)创新的流化床水泥生产工艺的扩大一个日产量为20吨的中试工厂扩大到日产量为200吨的大型工厂。在此放大过程中,主要设备的主要规格可根据热平衡计算进行设计。造粒床和煅烧床都是通过扩大其二维直径来扩大规模的,但需要进行一些修改才能实现平稳运行。
英文摘要
Results are classified into two subjects : (1) elucidation of solids circulation mechanism in spouted beds and (2) development of a scale-up method for fluidiized-bed cement production process.(1) Characteristics of particle circulation in a spouted bed with a draft tubeThe proposed cement production process using fluidization consists of two-stage fluidized beds. : one is upper spouted bed for granulation and the other is lower fluidized bed for calcination. In order to complete the calcination at 1300゚C without agglomeration trouble it is essential to produce homogeneous-sized granulus at the upper spouted bed.With this view a spouted bed of 0.205m diameter with a draft tube has been used to study the effect of gas velocity on the behavior of solids circulation. Based on visual observation using a borescope and the analyzes of pressure fluctuation and optical signals it was found that solid particles move from annulus into gas jet to from clusters periodically and are carried upward in the draft tube. At a certain maximum gas velocity, however, solids flow becomes homogeneous and are transported upward without cluster formation.(2) Scale-up of an innovative fluidizd-bed cement production processA pilot-plant with 20 tons per day was scaled up to a larger plant having the capacity of 200 t/d. In this scale-up process the principal specifications of main equipments could be designed on the basis of heat-balance calculation. Both granulating and calcinating beds were scaled up by enlarging their diameters twodimensionally, but several modifications were needed to achieve smooth operation.
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影响因子:
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作者:
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通讯作者:
H.Ji,A.Tsutsumi and K.Yoshida: "Studies on the solid Circulation in a Spouted Bed with a Draft Tube" Fifth Asian Conf.on Fluidized Bed and Three-phase Reactors. 5. 50-55 (1996)
H.Ji,A.Tsutsumi 和 K.Yoshida:“带有尾流管的喷动床中的固体循环研究”第五届亚洲流化床和三相反应器会议。
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通讯作者:
I.Hashimoto, K.Mukai and K.Yoshida: "Scale-up of Innovative Fluidized-Bed Cement Clinker Production Process" Second International Sym. on Scale Modeling. (1997)
I.Hashimoto、K.Mukai 和 K.Yoshida:“创新型流化床水泥熟料生产工艺的规模化”第二届国际研讨会
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通讯作者:
Kikuchi, T., R. Yamazaki, A. Tsutsumi and K. Yoshida: "Geanulation in a Fast Fluidized Bed" Fluidization VIII. 2. 1019-1025 (1995)
Kikuchi, T.、R. Yamazaki、A. Tsutsumi 和 K. Yoshida:“快速流化床中的颗粒化”流化 VIII。
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作者:
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通讯作者:
I.Hashimoto,K.Mukai and K.Yoshida: "Scale-up of Innovative Fluidized-Bed Cement Clinker Production Process" Second International Sym.on Scale Modeling. (1997)
I.Hashimoto、K.Mukai 和 K.Yoshida:“创新型流化床水泥熟料生产工艺的放大”第二届国际 Sym.on 规模建模。
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