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案例展示

工作原理

物(wu)(wu)(wu)(wu)(wu)(wu)料(liao)(liao)(liao)(liao)流(liu)程(cheng)是:水(shui)分80-85%物(wu)(wu)(wu)(wu)(wu)(wu)料(liao)(liao)(liao)(liao)先经(jing)过(guo)(guo)专用脱水(shui)机(ji)(ji)(ji),水(shui)分脱除到(dao)68%左右,由螺旋(xuan)输送机(ji)(ji)(ji)送入搅(jiao)拌(ban)(ban)滚筒烘干(gan)机(ji)(ji)(ji)实现顺流(liu)烘干(gan),物(wu)(wu)(wu)(wu)(wu)(wu)料(liao)(liao)(liao)(liao)在(zai)(zai)抄板下不断抄起(qi)、散落呈螺旋(xuan)行进(jin)式(shi)前进(jin),内(nei)(nei)置搅(jiao)拌(ban)(ban)桨叶装(zhuang)置将物(wu)(wu)(wu)(wu)(wu)(wu)料(liao)(liao)(liao)(liao)充(chong)(chong)分搅(jiao)拌(ban)(ban)打散破(po)碎(sui),充(chong)(chong)分扩(kuo)大(da)物(wu)(wu)(wu)(wu)(wu)(wu)料(liao)(liao)(liao)(liao)与(yu)热(re)(re)气(qi)热(re)(re)交换面积(ji),物(wu)(wu)(wu)(wu)(wu)(wu)料(liao)(liao)(liao)(liao)与(yu)热(re)(re)气(qi)充(chong)(chong)分质热(re)(re)交换,水(shui)分迅速蒸发汽化,达到(dao)35%左右,完成(cheng)(cheng)滚筒干(gan)燥过(guo)(guo)程(cheng),由螺旋(xuan)输送机(ji)(ji)(ji)排出,进(jin)入半湿(shi)物(wu)(wu)(wu)(wu)(wu)(wu)料(liao)(liao)(liao)(liao)专用粉碎(sui)机(ji)(ji)(ji),粉碎(sui)物(wu)(wu)(wu)(wu)(wu)(wu)料(liao)(liao)(liao)(liao)粒度到(dao)1mm以下,进(jin)入脉冲(chong)气(qi)流(liu)烘干(gan)过(guo)(guo)程(cheng),物(wu)(wu)(wu)(wu)(wu)(wu)料(liao)(liao)(liao)(liao)迅速降到(dao)12%以下。(可避免物(wu)(wu)(wu)(wu)(wu)(wu)料(liao)(liao)(liao)(liao)在(zai)(zai)烘干(gan)过(guo)(guo)程(cheng)中糊化、糖(tang)化现象(xiang)发生,造成(cheng)(cheng)物(wu)(wu)(wu)(wu)(wu)(wu)料(liao)(liao)(liao)(liao)外观颜(yan)色发黑(hei)),由旋(xuan)风卸料(liao)(liao)(liao)(liao)器和脉冲(chong)袋(dai)式(shi)收尘器回收干(gan)料(liao)(liao)(liao)(liao)粉,废气(qi)达标排放(fang),完成(cheng)(cheng)整个烘干(gan)过(guo)(guo)程(cheng)。滚筒内(nei)(nei)部(bu)安装(zhuang)有震打清理装(zhuang)置,防止物(wu)(wu)(wu)(wu)(wu)(wu)料(liao)(liao)(liao)(liao)与(yu)筒壁粘接。

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设备结构

设备选型

设备规格 处理量(t/h) 产出量(t/h) 原料水分(%) 干料水分(%) 总功率(kw) 总重量(kg) 占地面积(长*宽)
DLZG1610 2.25 0.5 80±5% 12%(可调) 125 50000 40m*12m
DLZG2010/3 4.5 1 185 60000 42m*15m
DLZG2510/3 6.75 1.5 225 70000 45m*15m
DLZG2910/3 9.0 2 280 80000 48m*15m
DLZG3210/3 11.25 2.5 335 90000 50m*15m
DLZG3510/3 13.5 3 380 100000 50m*15m
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