版权说明:本文档由用户提供并上传,收益归属内容提供方,若内容存在侵权,请进行举报或认领
文档简介
1、标准:锅炉房设计规范、设备及管道绝热技术通则、设备及管道绝热设计导则、动力管道设计手册、工业锅炉经济运行、锅炉节能技术监督管理规程保保温温层层经经济济厚厚度度计计算算管道外径(裸管外径)mDo0.108假设保温层厚度m0.127设备或管道外表面温度T250环境温度Ta12年运行时间 ht8000单位换热系数A10.0018975保温层外径(两层时为内层保温层外径)mD10.362热价 元/GJPE16保温材料制品热导率W/mk0.05498保温层单位造价 元/mP1400保护层单位造价 元/P215保温结构单位造价 元/mPT581.9400235年利率%(复利率)i10%计息年数 年n7保温
2、工程投资贷款年分摊率%(复利计算)S0.2054055管道外的風速 m/s0保温层外表面向大气的表面传热系数W/k11.63保温层厚度m0.127D1/Doln(D1/Do)=4.071931838D1/DO3.36附表校核保温层外径mD1j0.36288保温层厚度m0.12744保保温温层层厚厚度度计计算算(控控制制散散热热损损失失)管道外径(裸管外径)mDo0.108设备或管道外表面温度T250环境温度Ta12保温层内外表面平均温度Tm131富裕系数K0.9允许散热损失w/Q163保温材料制品热导率W/mk0.05498查表管道外的風速 m/s0保温层外表面向大气的表面传热系数W/k11.
3、63D1/Doln(D1/Do)=1.56D1/DO2.1查表保温层外径mD10.2268保保温温层层厚厚度度m m0.0594保保温温层层厚厚度度m(m(快快速速计计算算) )0.102保保温温层层厚厚度度计计算算(控控制制外外表表面面温温度度)管道外径(裸管外径)mDo0.108设备或管道外表面温度T200环境温度Ta25假设保温层外表面温度Ts50保温层内外表面平均温度Tm125保温材料制品热导率W/mk0.0539查表管道外的風速 m/s0保温层外表面向大气的表面传热系数W/k11.63对于防烫伤,则取8.141D1/Doln(D1/Do)=0.51D1/DO1.43查表保温层外径mD
4、10.15444保温层厚度m0.02322保保温温层层表表面面散散热热损损失失计计算算和和外外表表面面温温度度计计算算管道外径(裸管外径)mDo0.108假设保温层厚度m0.127设备或管道外表面温度(介质温度)T250环境温度Ta12年运行时间 ht8000单位换热系数A10.0018975保温层外径(两层时为内层保温层外径)mD10.362热价 元/GJPE16内层保温材料制品热导率W/mk10.05498保温层单位造价 元/mP1400保护层单位造价 元/P215保温结构单位造价 元/mPT581.94年利率%(复利率)i10%计息年数 年n7保温工程投资贷款年分摊率%(复利计算)S0.
5、21管道外的風速 m/s0保温层外表面向大气的表面传热系数W/k11.63保温层厚度m0.127D1/Doln(D1/Do)=4.07D1/DO3.36附表校核保温层外径mD1j0.363保温层厚度m0.127(T-Ta)/Do2203.70单层散热损失w/Q58.26单位管道长度散热损失w/mq66.22保温层外表面温度Ts17.01与假设保温层厚度接近,则正确标准:锅炉房设计规范、设备及管道绝热技术通则、设备及管道绝热设计导则、动力管道设计手册、工业锅炉经济运行、锅炉节能技术监督管理规程对于防烫伤,则取8.141架架 空空 蒸蒸 汽汽 管管 道道 保保 温温 计计 算算一、保温计算:硅酸铝
6、容重:380kg/m3蒸汽介质温度:按3000C导热系数=0.047+0.00012tpjtpj:管道内热介质和周围空气温度的平均值,周围空气温度取大值,10对蒸汽:导热系数=0.047+0.00012*(300+10)/2=0.0656W/m.K对蒸汽管道(架空)150200250300350400450外径mm159219273325377426478壁厚mm4.5668888允许每米热损失qkcal/m.h.K 0.450.530.620.670.750.820.86允许每米热损失qW/m167.47 197.245 230.74 249.35 279.12 305.17 320.058
7、导热系数W/m.K0.0656 0.06560.0656 0.0656 0.0656 0.0656 0.0656蒸汽介质温度oC300300300300300300300管道外表面热阻m.K/W0.0260.0260.0170.0170.0170.0170.017周围空气温度oC-20-20-20-20-20-20-20保温壳外径计算Dw mm345.63 422.723 480.01 547.59 600.37 651.59716.588保温壳厚度mm93.3101.9103.5111.3111.7112.8119.3设计保温层厚度mm111122124133134135143地地 沟沟 敷
8、敷 设设 蒸蒸 汽汽 管管 道道 保保 温温 计计 算算一、保温计算:硅酸铝容重:380kg/m3蒸汽介质温度:按3000C导热系数=0.047+0.00012tpjtpj:管道内热介质和周围空气温度的平均值,周围空气温度取大值,10对蒸汽:导热系数=0.047+0.00012*(300+10)/2=0.0656W/m.K对蒸汽管道(地沟,周围空气温度10度)150200250300350400450外径mm159219273325377426478壁厚mm4.5668888允许每米热损失qkcal/m.h.K 0.450.530.620.670.750.830.86允许每米热损失qW/m16
9、7.47 197.245 230.74 249.35 279.12 308.89 320.058导热系数W/m.K0.0656 0.06560.0656 0.0656 0.0656 0.0656 0.0656蒸汽介质温度oC300300300300300300300管道外表面热阻m.K/W0.0770.0690.060.0520.0430.0430.043周围空气温度oC10101010101010保温壳外径计算Dw mm314.37 390.077 446.99 513.65 568.25 616.15682.099保温壳厚度mm77.785.587.094.395.695.1102.0设计
10、保温层厚度mm931021041131141141225006007005296307208890.931.021.13346.109 379.603 420.54080.06560.06560.06563003003000.0170.0130.011-20-20-20768.835 886.825980.6310631119.9128.4130.31431541565006007005296307208890.931.071.13346.109 398.211 420.5408架架 空空 蒸蒸 汽汽 管管 道道 保保 温温 计计 算算地地 沟沟 敷敷 设设 蒸蒸 汽汽 管管 道道 保保 温温
11、 计计 算算0.06560.06560.06563003003000.0430.0320.029101010733.961 839.289945.1961175102.5104.6112.6122125135架架 空空 热热 油油 管管 道道 保保 温温 计计 算算一、保温计算:硅酸铝容重:75kg/m3热油介质温度:按3000C保温外表面40导热系数=0.038+0.00014tpjtpj:管道内热介质和周围空气温度的平均值,周围空气温度取大值,10对蒸汽:导热系数0.0597 W/m.K对热油管道(架空)15020025030012510080外径mm1592192733251331088
12、9壁厚mm4.5678444允许每米热损失qW/m186186186186186186186导热系数W/m.K0.0597 0.0597 0.05970.05970.05970.0597 0.0597热油介质温度oC300300300300300300300管道外表面热阻m.K/W0.0260.0260.0170.0170.0170.0170.017周围空气温度oC10101010101010保温壳外径计算Dwmm282.507389.113 486.698 579.403 237.109 192.54158.667保温壳厚度mm61.885.1106.8127.252.142.334.8设计
13、保温层厚度mm74102128152625041导热油管径DN30025020015012510080设计保温层厚度mm1501501501001005050地地 沟沟 敷敷 设设 热热 水水 管管 道道 保保 温温 计计 算算一、保温计算:硅酸铝容重:380kg/m3热水介质温度:按1300C导热系数=0.047+0.00012tpjtpj:管道内热介质和周围空气温度的平均值,周围空气温度取大值,10对热水:导热系数=0.047+0.00012*(130+10)/2=0.0554W/m.K对热水管道(地沟,周围空气温度10度)150200250300350400450外径mm15921927
14、3325377426478壁厚mm4.5668888允许每米热损失qkcal/m.h.K 0.791.041.011.171.341.51.66允许每米热损失qW/m110.252 145.142140.956 163.285 187.01209.34 231.67导热系数W/m.K0.0554 0.0554 0.05540.05540.05540.0554 0.0554蒸汽介质温度oC130130130130130130130管道外表面热阻m.K/W0.0860.0770.0690.060.0520.0430.039周围空气温度oC10101010101010保温壳外径计算Dwmm225.3
15、5284.271 358.402 411.017 462.849512.301564.677保温壳厚度mm33.232.642.743.042.943.243.3设计保温层厚度mm393951515151526550407657453.53.531861861860.05970.0597 0.05973003003000.0170.0130.011101010135.4911358 101.771 80.405729.722.417.73526216550405050505006007005296307208891.832.152.44255.3948300.054 340.526架架 空空
16、热热 油油 管管 道道 保保 温温 计计 算算地地 沟沟 敷敷 设设 热热 水水 管管 道道 保保 温温 计计 算算0.05540.0554 0.05541301301300.0340.0340.031101010615.6198384 715.535 805.18243.342.842.6515151x x與與xlnxxlnx函函數數表表( (當當x=1x=15 5時時的的xlnx)xlnx)值值x xxlnxxlnxx xxlnxxlnxx xxlnxxlnxx xxlnxxlnxx x10.0001.420.4992.141.632.863.0023.581.0050.0051.430.
17、5122.151.6482.873.0213.591.010.010051.440.5262.161.6652.883.0453.61.0150.015151.450.5392.171.6812.893.0653.611.020.02021.460.5522.181.6992.93.0853.621.0250.2531.470.5652.191.722.913.1043.631.030.03041.480.582.21.7352.923.133.641.0350.03561.490.5942.211.7562.933.153.651.040.04071.50.6072.221.7712.943
18、.173.661.0450.0461.510.6222.231.7912.953.193.671.050.05121.520.6372.241.8052.963.213.681.0550.05651.530.652.251.8252.973.243.691.060.06171.540.6652.261.8412.983.253.71.0650.0671.550.6792.271.8612.993.273.711.070.07241.560.6952.281.8833.293.721.0750.07771.570.7082.291.8993.013.313.731.080.08311.580.7
19、222.31.923.023.343.741.0850.08851.590.7372.311.9353.033.363.751.090.09461.60.7512.321.9553.043.383.761.0950.09941.610.7652.331.973.053.43.771.10.10481.620.7822.341.993.063.423.781.1050.111.630.7992.352.0073.073.443.791.110.11621.640.8152.362.0273.083.463.81.1150.121.1.650.8272.372.0423.093.483.811.1
20、20.127.1.660.8422.382.0623.13.53.821.1250.13271.670.8562.392.083.113.533.831.130.1381.680.8722.42.13.123.553.841.1350.1431.690.8892.412.123.133.573.851.140.14921.70.9022.422.143.143.593.861.1450.15451.710.9162.432.163.153.613.871.150.16071.720.9322.442.183.163.643.881.1550.16651.730.9492.452.1953.17
21、3.663.891.160.17211.740.9652.462.2173.183.683.91.1650.17721.750.982.472.2333.193.73.911.170.18461.760.9942.482.2553.23.723.921.1750.1891.771.0112.492.273.213.743.931.180.1951.781.0292.52.293.223.763.941.1850.2011.791.042.512.313.233.783.951.190.2071.81.0592.522.3283.243.813.961.1950.2131.811.0812.53
22、2.3443.253.833.971.20.2181.821.0892.542.373.263.853.981.2050.251.831.1082.552.3853.273.883.991.210.231.841.1212.562.4053.283.941.2150.2361.851.1382.572.4253.293.924.011.220.2421.861.1522.582.4443.33.944.021.2250.2451.871.1692.592.4623.313.964.031.230.25451.881.1852.62.483.323.984.041.2350.2611.891.2
23、052.612.5033.3344.051.240.2661.91.222.622.5213.344.034.061.2450.2721.911.2342.632.543.354.054.071.250.2791.921.2512.642.563.364.074.081.2550.2851.931.272.652.583.374.094.091.260.2911.941.2882.662.63.384.124.11.2650.2981.951.3022.672.623.394.144.111.270.341.961.3182.682.643.44.164.121.2750.3091.971.3
24、352.692.663.414.184.131.280.3161.981.3512.72.683.424.24.141.2850.3221.991.3692.712.73.434.234.151.290.32821.3862.722.723.444.254.161.2950.3342.011.4012.732.743.454.274.171.30.342.021.4192.742.763.464.34.181.310.3542.031.4392.752.783.474.324.191.320.3672.041.4552.762.83.484.344.21.330.382.051.4712.77
25、2.823.494.364.211.340.3892.061.4882.782.843.54.384.221.350.4052.071.5072.792.863.514.44.231.360.4172.081.522.82.883.524.424.241.370.4322.091.5422.812.9013.534.454.251.380.4452.11.5592.822.9213.544.474.261.390.4572.111.5792.832.943.554.54.271.40.472.121.5922.842.9613.564.524.281.410.4852.131.612.852.
26、983.574.554.29xlnxxlnxx xxlnxxlnx4.574.36.274.594.316.294.624.326.324.644.336.354.664.346.384.684.356.44.714.366.424.734.376.444.754.386.464.774.396.484.84.46.524.824.416.544.844.426.574.864.436.64.884.446.624.914.456.644.934.466.674.964.476.74.984.486.7254.496.745.034.56.775.054.516.795.074.526.815
27、.094.536.835.124.546.865.154.556.95.174.566.925.194.576.945.214.586.975.244.596.995.264.67.025.284.617.055.314.627.075.334.637.15.354.647.1253.74.657.145.44.667.165.434.677.195.454.687.215.474.697.245.54.77.265.534.717.285.554.727.325.574.737.355.64.747.385.624.757.45.644.767.425.664.777.455.684.787
28、.475.714.797.5x x與與xlnxxlnx函函數數表表( (當當x=1x=15 5時時的的xlnx)xlnx)值值5.744.87.525.764.817.555.784.827.585.814.837.65.834.847.635.854.857.655.884.867.685.914.877.75.934.887.735.954.897.765.984.97.786.014.917.86.034.927.836.054.937.856.074.947.866.14.957.96.134.967.926.154.977.956.174.9886.194.998.026.2258.
29、056.25附附表表2: 2:保保 溫溫 層層 平平 均均 溫溫 度度 tp tp周遭空氣溫度()介 質 溫 度10015020025030035040025709512515017520523015659012014517020022506080110135160190215-155575105130155185210附附表表3-1:3-1:季季 節節 運運 行行 工工 況況 允允 許許 最最 大大 散散 熱熱 損損 失失設備、管道及附件外表面溫度50100150200250300允許最大散熱損失116163203244279308附附表表3-2:3-2:常常 年年 運運 行行 工工 況況
30、允允 許許 最最 大大 散散 熱熱 損損 失失設備、管道及附件外表面溫度 323(50)373(100)423(150)473(200)523(250)573(250)允許最大散熱損失5893116140163186附附表表4: 4:保保 溫溫 層層 表表 面面 熱熱 阻阻公稱直徑(mm)室內室外介質溫度t()介質溫度t()100200300400500100200300圓 筒 面 放 熱 阻 力 R2 (m2K/w)250.3010.2580.2150.1980.1890.1030.0950.086320.2750.2320.1980.1630.1380.0950.0860.077400.2
31、580.2150.1810.1550.1290.0860.0770.069500.1980.1630.1380.120.1030.0690.060.0521000.1550.1290.1120.0950.0770.0520.0430.0431250.1290.1120.0950.0770.0690.0430.0340.0341500.1030.0860.0770.0690.060.0340.0260.0262000.0860.0770.0690.060.0520.0340.0260.0262500.0770.0690.060.0520.0430.0260.0170.0173000.0690.0
32、60.0520.0430.0430.0260.0170.0173500.060.0520.0430.0430.0430.0170.0170.0174000.0520.0430.0430.0340.0340.0170.0170.0175000.0430.0340.0340.0340.0340.0170.0170.0176000.0360.0340.0320.030.0280.0140.0130.0137000.0330.0310.0290.0280.0260.0130.0120.0118000.0290.0280.0250.0250.0230.0110.010.019000.0260.0250.
33、0250.0220.0220.010.0950.09510000.0230.0220.0220.0210.0210.0090.0860.08620000.0140.0130.0120.0110.010.0050.0040.004623(350)2094005000.0770.0770.0690.060.060.0520.0430.0430.0340.0340.0260.0260.0260.0260.0170.0170.0170.0170.0170.0170.0170.0170.0170.0170.0170.0170.0120.0110.010.010.0950.0950.0860.0860.0080.0080.0040.004常常 年年 運運 行行 工工 況況 允允 許許 最最 大大 散散 熱熱 損損 失失保保 溫溫 層層 表表 面面 熱熱 阻阻室外介質溫度t()圓 筒 面 放 熱 阻 力 R2 (m2K/w)保保温温材材料料参参考考标标准准说明: 1、导热系数越小越好。 2、氧指
温馨提示
- 1. 本站所有资源如无特殊说明,都需要本地电脑安装OFFICE2007和PDF阅读器。图纸软件为CAD,CAXA,PROE,UG,SolidWorks等.压缩文件请下载最新的WinRAR软件解压。
- 2. 本站的文档不包含任何第三方提供的附件图纸等,如果需要附件,请联系上传者。文件的所有权益归上传用户所有。
- 3. 本站RAR压缩包中若带图纸,网页内容里面会有图纸预览,若没有图纸预览就没有图纸。
- 4. 未经权益所有人同意不得将文件中的内容挪作商业或盈利用途。
- 5. 人人文库网仅提供信息存储空间,仅对用户上传内容的表现方式做保护处理,对用户上传分享的文档内容本身不做任何修改或编辑,并不能对任何下载内容负责。
- 6. 下载文件中如有侵权或不适当内容,请与我们联系,我们立即纠正。
- 7. 本站不保证下载资源的准确性、安全性和完整性, 同时也不承担用户因使用这些下载资源对自己和他人造成任何形式的伤害或损失。
最新文档
- 2024年度版权许可使用合同文学作品
- 二零二四年度企业级信息系统升级改造合同2篇
- 商铺转让合同
- 2024年度船舶物料供应合同2篇
- 2024年二手货车买卖合同规范3篇
- 2024年度技术开发合同新药研究2篇
- 2024年度城市供水供应系统维护合同3篇
- 弱电工程现场施工与管理合同20243篇
- 2024年度二手汽车交易服务合同
- 《新媒体运营》课件
- 2024年浙江省初中学业水平考试数学试题(潮汐卷)(解析版)
- 中职教育一年级上学期英语《We Are Friends》课件
- 专题10 议论文阅读(含答案) 2024年中考语文【热点-重点-难点】专练(上海专用)
- 21 小圣施威降大圣 公开课一等奖创新教案
- 新概念第四册课文翻译及学习笔记:Lesson5
- 业绩对赌协议范文(2024版)
- 宠物医院服务行业市场调研分析报告
- 中国金属门窗行业分类、市场运行态势及产业链全景图谱分析
- 环境治理与利益相关者参与
- 《第6单元 除数是两位数的除法:商是两位数的除法》课件
- JT∕T 795-2023 事故汽车修复技术规范
评论
0/150
提交评论