筒体壁厚计算

1、氢气量 小室数室电压（V） 电量电流（A） 发热量（kwh） 发热量（kcol） 碱循环量(m3/h)102239012.42810688.080.5959674365223906.2145344.040.29798371820022390248.56213761.611.9193487237522390466.0540080322.34877886填充容积计算图号外筒直径(米)内筒直径（米）当量直径（米）内筒高度（米）容积（米3）有效容积（米3）QCZ10/3.2-02-010.2070.1080.1771.440.0350.028QCZ25/3.2-030.2610.1080.2381.6

2、40.0730.058QCZ60/1.6-03-040.30.1330.2691.330.0750.060QCZ80/1.6-03-040.40.1590.3671.620.1710.137QCZ100/1.6-03-040.40.1590.3671.620.1710.137QCZ160/1.6-03C0.40.1590.3671.50.1590.127QCZ160/1.6-06-040.450.1590.4211.720.2390.191QCZ200/1.6-03-040.0000.0000.000QCZ250/1.6-03-040.40.1590.3671.570.1660.133QCZ5

3、00/1.6-03-040.50.1590.4741.70.3000.240QCZ700/1.6-03-040.50.1590.4741.60.2820.226QCZ750/1.6-03-040.60.1590.5791.970.5180.414QCZ1000/1.6-03-040.70.2730.6451.940.6330.506 0.2070.1080.1770.90.0220.018可装分子筛（kg）计算分子筛用量（kg）氢气实际体积空塔线速度2070.3360.00441130.8410.0054263.6070.01896214.8090.01396216.0120.01689406

4、.0120.01613440 04012.023#DIV/0!935015.0290.03916830.0580.04715842.0810.06629045.0870.04835460.1160.05112流量Q= D2Vt/4流速V（米/秒）管径D（毫米）流量Q（立方米/小时）流量Q（立方米/分钟）1100.28260.004711.55010.59750.1766252202.26080.037682.5254.4156250.073593753307.63020.127171.5252.6493750.0441562545028.260.471筒体壁厚计算 Pc Di受内压作用： S=

5、 2Kt - Pc设计压力Pc(Mpa)筒体内径Di(mm)焊接系数K许用应力t(Mpa)计算厚度S(mm)110000.9154 3.62056520R1.610000.9154 5.805515Q345R(16MnR)3.318001160 18.75592Q345RD(16MnDR)1.0518001157 6.0393033041.610000.9137 6.530612304L1.610000.9118 7.590133垫片压紧力p=6.28Dg b m pcDg(mm)b(mm)m垫片系数pc(Mpa)Fp(MN)10004.521.69043210004.521.690432螺栓

6、最大间距不宜超过L=2db+6f/m+0.5db(mm)f(mm)m垫片系数L1212252.81212252.8螺栓最小间距L螺栓直径LaLbLe螺栓最小间距L 螺栓直径 La12201616323044162420183836482030242046425622322624524860243427265656702738302862螺栓最小载荷W=F+FpDg(mm)pc(Mpa)F(MN)10001.61256000流速V=Q/SQ立方米/小时管径D(mm)SV米/秒1.6MPa3.2MPa0.65MPa700.390.11941628539580493521713.7850162016

7、9429.21502710020314886311.795232003280469429.215027300328041046313.8225425002504906314101.8872382250030070650886311.795231001079354221147.18094 安全泄放量：W2.83103pvd2安全阀安全放能力的计算：ASA/SndA/ns/d5000.132 1893.9391120.0282.231189200.258 1782.9462560.0281.8026716700.4321932.874320.0281.9346324800.685 1810.219

8、0.028 75846001.188 1936.02712560.0281.83134766001.673 1972.50416720.0281.97177282002.159 1899.02719840.0322.07189010600.258 2054.26419840.0320.2718905001250直径D厚度b单片体积n片总体积V(l)单片面积m2电流16.420.021 20.9532427457412.116489410014.460.021 16.2495513822421.641369330012.160.021 11.49138708041.16074523009.240

9、.0216.63512905970.67021412407.30.021 4.141432542240.4183278355.620.021 2.454582501230.24793846040.0211.2434446570.12565003.90.01 1.07458784900.1193992502.90.01 0.0924261010.066019260LbLe螺栓最小间距L35307038368042904810255116筒体壁厚计算 Pc Di受内压作用： S= 2Kt - Pc垫片压紧力p=6.28Dg b m pc螺栓最大间距不宜超过L=2db+6f/m+0.5螺栓最小间距L

10、螺栓最小载荷W=F+FpsDNA/N0.09290.00458060.04520.2090.004130630.04510.3630.004226880.04530.5940.004371250.03 1.0560.004660000.03531.3890.004868130.04521.9350.0041209380.03611.9350.0041209380.0061电流密度193720111981185019961855398120943938氢气产量（Nm3/hr）直流电流（A）电室计算数小电室数直流电压（V）55004546501092048505240248072747818046

11、001741781821506600101102104120460011611812237566002532542621504600145146150100460097981006024801081101121254600121122128301670808286催化剂用量的计算V 处理气体量（M3/h) 设计空速（小时-1）U 催化剂用量(M3)G 催化剂重量(kg)1050000.0021.5003050000.0064.50020050000.04030.00010050000.02015.00050050000.10075.0003500100000.350262.5001250500

12、00.250187.500125080000.156117.188脱氧器尺寸的计算V 处理气体量（M3/h)u气体线速度（米/秒）p工作压力（bar 绝压)U 催化剂用量(M3)500.180.0121000.1170.025000.1170.12000.1170.04吸附剂用量的计算V 处理气体量（M3/h)T 周期（小时）q 设计吸附容量g1含湿量（克/米3）700240.18.2700240.130.4500120.115.3610240.130.460240.18.23600360.17.521000240.18.2吸附器的直径DG 吸附剂用量（kg)Vg 吸附剂体积(M3)u空塔线速

13、度(米/秒）V 氢气的实际体积（M3）27.30.0340.051728.30.0350.051729.30.0370.051730.30.0380.051731.30.0390.051732.30.0400.051733.30.0420.0517810100210S 脱氧器截面积S=V/3600*u*p(M2)D 脱氧器直径（M)H 有效高度（M）Z 径高比0.0170.1490.6914.650.0160.1441.2248.480.0820.3231.2243.790.0330.2041.2246.00工作压力进气温度V 实际体积（M3）G 吸附剂用量G=g1*V*T/q(kg)G 吸附剂用量G=1.3G16644.71287.992114.4161546.154336.738437.8173032.64460.16978.233300.3362.4543.21663.8327.5429.81.1563199.2368660.97011259.316663.874125.703163.4D 吸附器直径（M）S 吸附器截面积（M