4初步设计说明书附录VIP

300兆瓦机组烟气脱硫工程目录内容附录一物料平衡表-2-1.1全过程物料平衡-1-1.2预处理部分-4-1.2.1喷淋塔T0101- 4-1.2.2冷凝器E0101- 5-1.3脱硫和氧化部分-6-1.3.1产品吸收塔T0201- 6-1.3.2深度脱硫塔T0202- 7-1.3.3反应器R0201- 8-1.4 MVR蒸发段-9-1.4.1热交换器E0301- 9-1.5结晶固液分离部分-10-1.5.1固液分离器CY0401- 10-1.6脱碳段-11-1.6.1冷凝器E0501- 11-1.6.2冷凝器E0502- 12-1.6.3加热器E0503- 13-1.6.4冷凝器E0504- 14-附录2能量平衡表-15-2.1总过程能量平衡-15-2.2预处理部分-16-2.2.1喷淋塔T0101- 16-2.2.2冷凝器E0101- 17-2.3脱硫和氧化部分-18-2.3.1产品吸收塔T0201- 18-2.3.2深度脱硫塔T0202- 19-2.3.3反应器R0201- 20-2.4 MVR蒸发段-21-2.4.1热交换器E0301- 21-2.5结晶固液分离部分-22-2.5.1加热器E0401- 22-2.5.2热交换器E0402- 23-2.5结晶固液分离部分-24-2.5.1固液分离器CY0401- 24-2.6脱碳段-25-2.6.1冷凝器E0501- 25-2.6.2冷凝器E0502- 26-2.6.3加热器E0503- 27-2.6.4冷凝器E0504- 28-附录3设备选择清单29表3-1塔架选择列表29表3-2换热器类型选择表29表3-3反应器选择列表30表3-4泵选择列表31表3-5压缩机选择列表31表3-7气液分离器选型表33表3-8模具选择列表33表3-9离心机选择列表33表3-10水力旋流器类型选择表33表3-11管道选择列表3437棒棒糖队300兆瓦机组烟气脱硫工程附录一物料平衡表1.1物料平衡的全过程表1-1全过程进口物流数据表溪流01010205021402170504温度1402525256压力棒1.11.0132511.421.01325蒸汽压裂10010摩尔流量千摩尔/小时44615.04200017006112000质量流量千克/小时130614035999.3430502.5217651.9435823.43体积流量累计/小时151212036.4531.9810670.2237.92焓Gcal/hrMMBtu/h-545.65-135.06-109.93-0.0014-126.82质量流量千克/小时SO24287.380000NH30537.69125.2203579.73N290687100476.580H2O57741.5735456.921574.48032238.32O215329900134.420二氧化碳1839410000总千克/小时1427117.23表1-2全流程出口物流数据表溪流02190408040905080509温度66666659.725.73压力棒1.11.013251.0132511蒸汽压裂10010摩尔流量千摩尔/小时754.87406.3422.7141640.217727.65质量流量千克/小时1984.3510602.342293.461243376.27149260.39卷流量累计/小时19319.849.111.691151882.65142.24焓Gcal/小时-10-31.12-6.35-391.46-543.54质量流量千克/小时SO219884.352440000NH3111.5460200042.92N20.00055939100906868.69492.37H2O13350.747915327.250.889575.976913130616.18O23134.15146300153297.8520.82二氧化碳3266.71010100173633.72359.22NH421.196384431223.180.2104338.09H00.8200NH2COO-0000675.59碳酸氢盐-000013056.95哦-00000.0015高铁酸盐-00000.78CO32-0000427.79SO32-000039.68SO42-0257.53000硫酸00000高铁酸盐-01492.780.2500SALT6002991.6900总千克/小时1427516.81表1-3全过程物料平衡表在在外质量流量千克/小时1427117.231427516.81从表1-3中可以看出，进出物料的整体质量是平衡的。1.2预处理部分1.2.1喷雾塔T0101表1-4 T0101输入和输出流列表在在外溪流0102022001030105温度C95.86648.9849.41压力棒1.11.11.11.1蒸汽压裂1010摩尔流量千摩尔/小时44615.043168.5646189.141594.86质量流量千克/小时1306139.3262126.291334499.6233766体积流量/小时1243501.0759.991123241.65焓Gcal/小时-560.19-219.50-666.15-113.54质量流量千克/小时SO24287.382.434291.590.87NH300.000330.0047N2906871.150.36906871.350.16H2O57741.5753849.8186098.5125493.61O2153298.650.15153298.760.049二氧化碳183940.570.021183939.391.19H2040.672040.67SO42-4798.344835.79高铁酸盐-1428.221390.391.2.2冷凝器E0101表1- 5 E0101进出料流股表在在外溪流01010102温度C14095.8压力棒1.11.1蒸汽压裂11摩尔流量千摩尔/小时44615.0444615.04质量流量千克/小时13061401306139.32体积流量累计/小时15121201243501.07焓Gcal/小时-545.65-560.19质量流量千克/小时SO24287.384287.38NH300N2906871906871.15H2O57741.5757741.57O2153299153298.65二氧化碳183941183940.571.3脱硫氧化工段1.3.1产品吸收塔T0201表1-6 T0201进出料流股表在在外溪流0104021102010212温度C48.9840.54741.9241.34压力棒1.11.11.013251.01325蒸汽压裂1010摩尔流量千摩尔/小时44615.077043.4344920.096683.46质量流量千克/小时1306138.94131605.691309020.26128717.41体积流量/小时1085195.62128.591160103.78124.00焓Gcal/小时-575.46-474.95-593.08-457.29质量流量千克/小时SO24286.730700.176.19NH301757.20546.398.89N2906871.350.78906871.250.88H2O57742.71120839.5863671.08113898.81O2153298.760.25153298.730.28二氧化碳183939.40.0052183932.626.79NH42791.414064.08H1.29NH2COO-26.1126.13碳酸氢盐-17.7217.73哦-0.13高铁酸盐-16.603251.85CO32-5.045.05SO32-6150.857429.431.3.2深度脱硫塔T0202表1-7 T0202进出料流股表在在外溪流0201020702020203温度C41.92938.9741.3741.69压力棒1.013251.11.013251.01325蒸汽压裂1010摩尔流量千摩尔/小时44920.0910009.8644907.3210013.03质量流量千克/小时1309020.26182977.221308284.93183722.35体积流量/小时1160103.78181.691157755.98182.33焓Gcal/小时-593.08-680.52-591.82-681.83质量流量千克/小时SO2700.17438.3625.530.54NH3546.391.38748.0630.90N2906871.25177549.34906870.901.72H2O63671.080.4463423.55177617.41O2153298.720.08153298.610.55二氧化碳183932.611535.87183918.