蒸馏塔与裙座的机械设计快速计算-excel 计算程序.xls
m016961228174017401589.92006993.92计算压力PcPc=P+Ph=p=
m021154.5351731.8031731.803004618.14圆筒计算厚度δδ=PcDi/(2[δ]t-Pc)=
m03224.7716.2831716.2831716.2831002373.55圆筒设计厚度δcδc=δ+C=
m0480120734.38491268.771268.77003471.92圆筒名义厚度δnδn=
m05327.58013353.8171796.6881796.688007274.77圆筒有效厚度δeδe=δn-C=
ma174307435435397.48001748.48 封头计算厚度δhδh=PcDi/(2[δ]t-0.5Pc)=
mw4217696.9027696.9026640.0970022454.9封头设计厚度δhcδhc=δh+C=
me1400260004000封头名义厚度δhnδhn=
0封头有效厚度δheδhe=δhn-C=
0.2*m02101.788220.54220.5400542.868
人孔分布122005塔设备质量载荷计算
M0(mi)9502207.289534.02110288.547500.9440030480.8塔段内直径Di1400
00塔段名义厚度δni10
Mmin9501879.75256.5757106.4144318.8140019511.5塔体高度H120000
Mmax9502300.713877.1116188.7612344.350045660.9单位筒体质量m1m348
塔盘个数分布1015150040筒体高度H1（总高-裙座-2*封头-底线）14040
塔段长度li200030005000500050000020000筒体质量m14885.92
验证封头质量m2368
M0(mi)30480.8裙座高度H35000
Mmin19130.7裙座质量m31740
Mmax45660.9
塔体自振周期T1=90.33H(mo*H/(E*δe*Di^3)^0.5*10^(-3)0.698066156
http://www.youqichuyun.com/xwb/images/bgimg/icon_logo.png 该贴已经同步到 helloshigy的微博 简单好用，好 简单好用，好 谢谢分享
谢谢楼主的分享
页:
[1]