Waste Heat Recovery Boiler Introduction

Waste Heat Recovery Boiler Introduction
1 / 33 PagesView full catalog

Waste Heat Recovery Boiler Introduction

Product catalog summary

Introduction

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.

Main Products

  • SLC300-23.5-4.0/400
  • SLC400-32-4.0/400
  • SLC500-42-4.0/400
  • SLC600-54-4.0/450
  • SLC800-68-5.3/485
  • SLC550-54.5-4.0/450

Engineering Project Examples and Key Parameters

Four representative projects illustrate the application and performance of Taishan WHRBs:

  • Chongqing Kaixian 2×300t/d Boiler: 300 tons/day waste capacity, 23.5 t/h steam evaporation, 4.0 MPa steam pressure, 400 °C steam temperature, 130 °C feedwater temperature, 80% efficiency, Kangheng grate. Thermal calculations show ~81% efficiency with detailed heat loss analysis.
  • Jinxiang 2×400t/d Boiler: 400 tons/day capacity, 32 t/h steam evaporation, 4.0 MPa/400 °C steam, 130 °C feedwater, 80.01% efficiency, Guangda grate. Includes detailed flue gas composition and heat transfer data; spray water desuperheating used for steam temperature control.
  • Haiyang 500t/d Boiler: 500 tons/day, 42 t/h steam evaporation, 4.0 MPa/400 °C steam, 130 °C feedwater, 80.2% efficiency, Kangheng grate. Thermal balance and spray water desuperheating maintain stable steam temperature and low heat losses.
  • Taian 2×600t/d Boiler: 600 tons/day, 54 t/h steam evaporation, 4.0 MPa/450 °C steam, 150 °C feedwater, 80% efficiency, Ebara grate. Thermal calculations show ~80.4% efficiency with detailed heat transfer data; spray water desuperheating applied; feedwater pressure 5.05 MPa, drum pressure 4.8 MPa.

Thermal Calculation and Heat Transfer Analysis

Each project includes comprehensive thermal balance calculations covering:

  • Boiler rated capacity and load rate
  • Steam output temperature and pressure
  • Feedwater temperature and pressure
  • Fuel composition and lower heating value
  • Theoretical air and combustion gas volumes
  • Heat losses: flue gas, incomplete combustion, mechanical, ash, radiation
  • Boiler efficiency and heat absorption by furnace walls, superheaters, economizers, evaporative convection bundles
  • Heat transfer coefficients for radiation and convection on flue gas and water/steam sides
  • Spray water desuperheating parameters for steam temperature control

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.

Key Technical Specifications and Parameters

  • Steam pressures typically at 4.0 MPa; drum pressures slightly higher (4.6–5.5 MPa)
  • Steam temperatures range from 400 °C to 450 °C depending on model
  • Feedwater temperatures between 130 °C and 150 °C
  • Boiler efficiencies around 80% to 82%
  • Flue gas discharge temperatures maintained near 190 °C
  • Fuel lower heating values approximately 6280–6700 kJ/kg
  • Use of spray water desuperheating for precise steam temperature control
  • Boiler grates supplied by reputable manufacturers (Kangheng, Guangda, Ebara)

Recommendations and Best Practices

  • Continuous monitoring of flue gas composition and temperature to optimize combustion and heat recovery
  • Ensure proper operation and maintenance of spray water desuperheaters for steam temperature control
  • Regular inspection and upkeep of boiler grates to maintain efficient fuel combustion
  • Use detailed thermal balance calculations to identify and minimize heat losses
  • Apply accurate heat transfer coefficients and flow parameters for design and operational optimization

Heat Transfer Parameters and Calculations

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.

Summary of Heat Transfer Component Calculations

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.

Waste Heat Boiler Design Proposals

  • 550T Waste Heat Boiler: 550 tons/day capacity, 54.5 t/h rated evaporation, 450 °C steam output, 130 °C feedwater, 7116 kJ/kg design heat value, 190 °C flue gas discharge, 80.2% efficiency, 4.0 MPa steam pressure.
  • 800T Waste Heat Boiler: 800 tons/day capacity, 68 t/h rated evaporation, 485 °C steam output, 150 °C feedwater, 6700 kJ/kg design heat value, 190 °C flue gas discharge, 83% efficiency, 5.3 MPa steam pressure.

Thermal Calculation Summary for 800T/D Boiler

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.

Key Observations and Recommendations

  • Heat transfer coefficients vary significantly with pipe specifications and operating conditions, affecting overall boiler efficiency.
  • Maintaining optimal flue gas and working fluid temperatures is essential for maximizing heat absorption and minimizing thermal losses.
  • Pollution/utilization coefficients impact heat transfer effectiveness and should be monitored to ensure system cleanliness and performance.
  • Design parameters such as feedwater temperature, steam output temperature, and pressure are tailored to waste disposal capacity and fuel characteristics.
  • Regular thermal balance checks and error analysis are recommended to validate calculation accuracy and operational stability.

Summary

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.

See more

Catalog excerpts

Waste Heat Recovery Boiler Introduction-1

泰山集团垃圾余热锅炉介绍 Waste Heat Recover

 Open the catalog to page 1
Waste Heat Recovery Boiler Introduction-2

泰山集团垃圾余热锅炉产品: Main Product

 Open the catalog to page 2
Waste Heat Recovery Boiler Introduction-4

—工程实例 我公司签

 Open the catalog to page 4
Waste Heat Recovery Boiler Introduction-5

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
Waste Heat Recovery Boiler Introduction-7

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
Waste Heat Recovery Boiler Introduction-8

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
Waste Heat Recovery Boiler Introduction-11

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
Waste Heat Recovery Boiler Introduction-13

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
Waste Heat Recovery Boiler Introduction-14

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
Waste Heat Recovery Boiler Introduction-18

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
Waste Heat Recovery Boiler Introduction-20

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
Waste Heat Recovery Boiler Introduction-21

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
Waste Heat Recovery Boiler Introduction-25

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
Waste Heat Recovery Boiler Introduction-28

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
Waste Heat Recovery Boiler Introduction-29

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
Waste Heat Recovery Boiler Introduction-30

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
Waste Heat Recovery Boiler Introduction-31

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 31
*Prices are pre-tax. They exclude delivery charges and customs duties and do not include additional charges for installation or activation options. Prices are indicative only and may vary by country, with changes to the cost of raw materials and exchange rates.