

This document provides a detailed overview of Taishan Group's Waste Heat Recovery Boilers (WHRB) designed for municipal solid waste incineration plants. It covers product models, engineering project examples, and comprehensive thermal calculation results focused on efficient steam generation from waste heat.
Four representative projects illustrate the application and performance of Taishan WHRBs:
Each project includes comprehensive thermal balance calculations covering:
Heat transfer components analyzed include furnace walls, multiple superheater stages, evaporative convection bundles, economizers, and convection wall tubes. Parameters such as gas and steam temperatures, enthalpy, flow rates, velocities, and heat transfer coefficients are tabulated to verify thermal balance with minimal relative errors.
Detailed heat transfer coefficients and parameters are provided for various boiler components, including radiation and convection coefficients on flue gas and working fluid sides. Key parameters include pollution/utilization coefficients, heat transfer coefficients (radiation and convection), overall heat transfer coefficients, average temperatures and pressures, heat transfer quantities, and relative error percentages. These are tabulated for different pipe specifications and operating conditions, illustrating variations in heat transfer performance and efficiency.
Calculations for evaporative convection tube bundles, wall tubes, and economizer tubes include tube specifications, convective heat transfer areas, flue gas inlet/outlet temperatures, enthalpy values, and flow rates/velocities of flue gas and working fluid. This provides a comprehensive overview of thermal performance and heat absorption efficiency across boiler sections.
Includes tube specifications for various boiler sections, heat transfer areas for radiation channels, evaporators, superheaters, and economizers, flue gas and working fluid temperatures, average velocities, main steam flow rate (68 t/h), and primary/secondary desuperheating water flow rates (0.95 t/h and 1 t/h). This data is critical for evaluating boiler performance and optimizing heat exchange efficiency.
Taishan Group's waste heat recovery boilers are engineered for efficient steam generation from municipal solid waste incineration. The document provides detailed technical data, thermal calculations, and operational parameters for multiple boiler models and projects. Emphasis is placed on maintaining high boiler efficiency (~80%), controlling steam parameters, and minimizing heat losses through precise thermal management and component design.
泰山集团垃圾余热锅炉介绍 Waste Heat Recover
Open the catalog to page 1泰山集团垃圾余热锅炉产品: Main Product
Open the catalog to page 2—工程实例 我公司签
Open the catalog to page 4相关参数 Data — 处理量Waste Disposal Capacity:300t/d — 额定蒸发量Rated Capacity:23.5t/h — 额定蒸汽出口压力Steam Output Pressure:4.0MPa — 额定蒸汽出口温度Steam Output Temperature:400℃ — 锅炉给水温度Boiler Feedwater Temperature:130℃ — 设计热值Design Heat Value
Open the catalog to page 5传热部件计算结果汇总 名称及符号 锅炉额定蒸发量Rated CapacityDe 额定蒸汽出口温度Steam Output Temperaturetgr
Open the catalog to page 7传热部件计算结果汇总 名称及符号 对流受热面积
Open the catalog to page 8相关参数 Data — 处理量Waste Disposal Capacity量:400t/d — 额定蒸发量Rated Capacity:32t/h — 额定蒸汽出口压力Steam Output Pressure:4.0MPa — 额定蒸汽出口温度Steam Output Temperature:400℃ — 锅炉给水温度Boiler Feedwater Temperature:130℃ — 设计热值Design Heat Value
Open the catalog to page 11连续排污率Ppw 出口蒸汽压力pgr 传热部件计算结果汇总 名称及符号 二级减温器 名称及符号 烟气出口焓 工质进口温度 工质出口温度 工质进口焓 工质出口焓 烟气流量 工质流量 烟气平均速度
Open the catalog to page 13传热部件计算结果汇总 名称及符号 管子规格 对流受热面积 烟气进口温度 烟气出口温度 烟气进口焓 烟气出口焓 工质进口温度 工质出口温度 工质进口焓 工质出口焓 烟气流量 工质流量 烟气平均速度 工质平均速度 过 热 器 3 二级过热 过 热 器 2 一级过热 过 热 器 1 蒸发对流 包墙管 器 包墙管 器 包墙管 管束2 m/s 污染系数或利用系数 m2.℃/W / 烟气侧辐射放热系数 W/℃.m2 / 烟气侧对流放热系数 W/℃.m2 /
Open the catalog to page 14相关参数 Data — 处理量Waste Disposal Capacity量:500t/d — 额定蒸发量Rated Capacity:42t/h — 额定蒸汽出口压力Steam Output Pressure:4.0MPa — 额定蒸汽出口温度Steam Output Temperature:400℃ — 锅炉给水温度Boiler Feedwater Temperature:130℃ — 设计热值Design Heat Value
Open the catalog to page 18热力计算结果汇总表 传热部件计算结果汇总 出口蒸汽流量D 入口水压力pgs 入口水温度tgs 锅筒工作压力pgt 连续排污率Ppw 出口蒸汽压力pgr 余热烟气参数 名称及符号 余热烟气密度ρ 外加热量Qwj 名称及符号 喷水水温tps 燃 烬 室 1 燃 烬 室 2 燃 烬 室 3 蒸发对流 对流包墙 过热器三 (汽水) (汽水) (汽水) 管束1 管 /
Open the catalog to page 20传热部件计算结果汇总 名称及符号 对流受热面积 烟气进口温度 烟气出口温度 过热器包 过热器包 过热器包 蒸发对流 过热器二 过热器一 墙管 墙管 墙管 管束2 烟气进口焓 烟气出口焓 工质进口温度 对流包墙 蒸发对流 对流包墙 省煤器 管 管束3 管 对流受热面积 烟气进口温度 烟气出口温度 烟气进口焓 烟气出口焓 工质进口温度 工质出口温度 工质进口焓 工质出口焓 工质出口温度 工质进口焓 工质出口焓 烟气流量 工质流量 烟气平均速度 烟气流量 工质流量 烟气平均速度
Open the catalog to page 21相关参数 Data — 处理量Waste Disposal Capacity量:600t/d — 额定蒸发量Rated Capacity:54t/h — 额定蒸汽出口压力Steam Output Pressure:4.0MPa — 额定蒸汽出口温度Steam Output Temperature:450℃ — 锅炉给水温度Boiler Feedwater Temperature:150℃ — 设计热值Design Heat Valu
Open the catalog to page 25入口水压力pgs 连续排污率Ppw 锅筒工作压力pgt 出口蒸汽温度tgr 名称及符号 烟气容积百分数CO 余热烟气密度ρ 外加热量Qwj 减温器类型 喷水压力Pps 喷水减温 MPa(g) 名称及符号 喷水水温tps 燃 烬 室 1 燃 烬 室 2 对流包墙 蒸发对流 过热器包 过热器二 (汽水) (汽水) 管 管束1 墙管 /
Open the catalog to page 28传热部件计算结果汇总 名称及符号 过热器包 过热器包 过热器包 过热器三 过热器一 墙管 墙管 墙管 烟气进口温度 烟气出口温度 烟气进口焓 烟气出口焓 工质出口温度 工质进口焓 工质出口焓 烟气流量 工质流量 烟气平均速度 污染系数或利用系数 m2.℃/W 烟气侧辐射放热系数 W/℃.m2 烟气侧对流放热系数 W/℃.m2 工质侧对流放热系数 W/℃.m2 传热系数 平均温压 辐射传热量 对流传热量 热平衡吸热量 相对误差 蒸发对流 蒸发对流 蒸发对流 蒸发对流 省煤器 管束2 包墙管 管束3 包墙管 Φ51×5 / 790
Open the catalog to page 29泰山集团部分垃圾焚烧炉方案设计 Design Proposal 一:550T垃圾余热锅炉 垃圾处理量Waste Disposal Capacity: 550T/D 额定蒸发量Rated Capacity:54.5T/h 蒸汽出口压力Steam Output Pres:4.0MPa 额定蒸汽出口温度 Steam Output Temp: 450℃ 额定给水温度Feedwater Temp:130℃ 设
Open the catalog to page 30泰山集团部分垃圾焚烧炉方案设计 Design Proposal 二:800T垃圾余热锅炉 垃圾处理量Waste Disposal Capacity: 800T/D 额定蒸发量Rated Capacity:68T/h 蒸汽出口压力Steam Output Pres :5.3MPa 额定蒸汽出口温度 Steam Output Temp: 485℃ 额定给水温度Feedwater Temp :15
Open the catalog to page 3143 Pages
1 Page
1 Page
1 Page
1 Page
1 Page
1 Page
1 Page
1 Page
1 Page
1 Page
1 Page
9 Pages
8 Pages
4 Pages
56 Pages
49 Pages
20 Pages
42 Pages
14 Pages
28 Pages
2 Pages