循环流化床锅炉发电机组与垃圾、污水处理一体化耦合能效分析

Energy efficiency analysis of integrated coupling between circulating fluidized bed boiler generator unit and garbage and sewage treatment

  • 摘要: 为降低燃煤发电过程中的CO2排放、水资源消耗、提高垃圾焚烧发电效率,同时提高采用生物法处理污水时的速度和效率,提出将垃圾、污水处理与循环流化床发电机组相结合的耦合系统。在循环流化床锅炉机组旁边分别建设厌氧发酵、生活和工业污水处理系统,其中厌氧发酵系统用于处理食品工业及农林畜牧等行业废弃物;生活和工业污水处理系统则分别用于处理生活污水和工业污水,发酵及污水处理过程中需要的热量来源于汽轮机低温抽汽或排汽余热。发酵产生的沼气耦合燃煤机组发电,沼渣用于生产有机肥料,生活污泥可与燃煤在流化床锅炉内混烧,工业污泥可根据其成分选择入炉混烧或无害化处理。不适合发酵降解的可燃垃圾经过预处理后直接送入流化床锅炉与燃煤进行混烧。对某2×350 MW超临界循环流化床机组耦合垃圾焚烧与污水处理系统后的项目进行了能效计算、应用场景以及收益分析,结果表明:对于人口规模达100万的城市,年生活垃圾焚烧可减少机组标煤消耗11.59万~19.32万 t,减少二氧化碳排放30.83万~51.39万t;在沼气利用方面,可与燃煤在炉内直接混烧发电,或利用燃机与燃煤机组进行排烟耦合或蒸汽耦合发电。随着燃机容量的增大,耦合系统的发电效率不断提高,同等条件下,排烟耦合的效率高于蒸汽耦合。该耦合系统还具有节约水资源、降低发酵设施建设成本、节约土地及总投资以及申请财政补贴等多方面收益。综上,循环流化床机组耦合垃圾焚烧、污水处理系统后环境及社会效益显著,尽管该种方式可能面临跨行业、跨部门等现实困难,但仍然值得进一步研究,特别是在新城区的规划建设方面,更具实施潜力。

     

    Abstract: In order to reduce CO2 emissions and water consumption in coal-fired power generation, improve the efficiency of waste-to-energy incineration, and enhance the speed and efficiency of biological wastewater treatment, a coupled system integrating waste and sewage treatment with circulating fluidized bed power units is proposed. Specifically, anaerobic fermentation, domestic and industrial wastewater treatment systems are constructed alongside the circulating fluidized bed boiler units. The anaerobic fermentation system is designed to handle waste from the food industry, agriculture, and livestock sectors, while the domestic and industrial wastewater treatment systems treat sewage and industrial wastewater respectively. The heat required for fermentation and wastewater treatment is sourced from low-pressure steam extraction or exhaust waste heat from turbines. The biogas produced from fermentation is coupled with coal-fired power generation, while the sludge is used to produce organic fertilizers. Domestic sludge can be co-fired with coal in the fluidized bed boiler, and industrial sludge can be either co-fired or treated for harmlessness based on its composition. Combustible waste unsuitable for fermentation is preprocessed and directly fed into the fluidized bed boiler for co-firing with coal. A case study was conducted on a 2×350 MW supercritical circulating fluidized bed unit coupled with waste incineration and wastewater treatment systems. Energy efficiency calculations, application scenarios, and benefit analyses were performed. The results indicate that for a city with a population of 1 million, annual waste-to-energy incineration can reduce standard coal consumption by 115 900−193 200 t and CO2 emissions by 308 300−513 900 t. In terms of biogas utilization, it can be directly co-fired with coal in the furnace for power generation, or coupled with gas turbines and coal-fired units through flue gas or steam integration. As the gas turbine capacity increases, the power generation efficiency of the coupled system continues to improve. Under the same conditions, flue gas coupling yields higher efficiency than steam coupling. The coupled system also offers additional benefits such as water conservation, reduced construction costs for fermentation facilities, land and total investment savings, and eligibility for financial subsidies. In summary, the integration of circulating fluidized bed units with waste incineration and wastewater treatment systems delivers significant environmental and social benefits. Although this approach may face practical challenges such as cross-industry and cross-departmental coordination, it remains worthy of further research, particularly in the planning and development of new urban areas, where it holds greater implementation potential.

     

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