刘建禹, 邓斯文, 杨胜明, 管延萱. 寒区低能耗厌氧发酵反应器热工性能参数研究[J]. 农业工程学报, 2019, 35(17): 248-255. DOI: 10.11975/j.issn.1002-6819.2019.17.030
    引用本文: 刘建禹, 邓斯文, 杨胜明, 管延萱. 寒区低能耗厌氧发酵反应器热工性能参数研究[J]. 农业工程学报, 2019, 35(17): 248-255. DOI: 10.11975/j.issn.1002-6819.2019.17.030
    Liu Jianyu, Deng Siwen, Yang Shengming, Guan Yanxuan. Study on thermal performance parameters of low-energy anaerobic fermentation reactor in cold region[J]. Transactions of the Chinese Society of Agricultural Engineering (Transactions of the CSAE), 2019, 35(17): 248-255. DOI: 10.11975/j.issn.1002-6819.2019.17.030
    Citation: Liu Jianyu, Deng Siwen, Yang Shengming, Guan Yanxuan. Study on thermal performance parameters of low-energy anaerobic fermentation reactor in cold region[J]. Transactions of the Chinese Society of Agricultural Engineering (Transactions of the CSAE), 2019, 35(17): 248-255. DOI: 10.11975/j.issn.1002-6819.2019.17.030

    寒区低能耗厌氧发酵反应器热工性能参数研究

    Study on thermal performance parameters of low-energy anaerobic fermentation reactor in cold region

    • 摘要: 厌氧发酵反应器是沼气工程中的核心装置,研究寒区低能耗厌氧发酵反应器,不仅有助于降低沼气工程的能量损耗,提高耗能与产能的产出比,而且对大中型沼气工程在北方寒冷地区的推广与应用尤为重要。低能耗厌氧发酵反应器围绕的核心问题就是在保证反应器厌氧发酵功能的前提下,能的"量"和"质"合理有效利用程度。该文以建筑于地上全混合式厌氧发酵反应器为研究对象,采用能量分析和?分析方法,从反应器的体形、围护结构保温性能以及低?供热方式等方面对寒区低能耗厌氧发酵反应器节能特性进行了分析和研究,得到了低能耗厌氧发酵反应器最佳体形为高径比为1∶2的圆柱形;提出了哈尔滨、沈阳、北京地区在冬季室外计算温度下不同规模节能型反应器顶部、侧壁围护结构导热热阻的阈值;中温厌氧发酵反应器低?热水供热系统进出口温度分别为45和38 ℃,供热系统?效率为86%,反应器供能与用能间能级差为0.018,表明能级匹配合理,用能效率较高。该研究结论可为今后寒区低能耗厌氧发酵反应器的节能设计提供参考依据。

       

      Abstract: Abstract: Anaerobic fermentation reactor is the core device of biogas projects. The study of low-energy anaerobic fermentation reactor in cold region is not only helpful to reduce the energy loss of biogas projects and to improve the output ratio of energy consumption and productivity, but also particularly important for the promotion and application of large and medium-sized biogas projects in cold northern China. The key issue about the low-energy anaerobic fermentation reactor is how to reasonably and effectively utilize "quantity" and "quality" of energy under the premise of ensuring the function of the reactor. In this paper the full hybrid anaerobic fermentation reactor built on the ground is taken as the research object. According to the method of energy analysis and exergy analysis, the author analyzes the energy-saving characteristics of low-energy anaerobic fermentation reactor in cold region in terms of the geometry analysis and the performance of envelope thermal insulation and the heating method of low-exergy. In this paper, the key problem of anaerobic fermentation reactor design is solved by using the concept of building shape coefficient. First, the shape of the reactor cross section is determined and 3 types of the reactor body shape coefficient models are established and solved by numerical analysis. The calculation results show that the optimal shape of the low-energy anaerobic fermentation reactor is cylindrical, and the aspect ratio is 1:2. Second, based on heat transfer theory, the thermal conductivity models of the difference of the volume of the reactor envelope structure are established by statistical method and numerical analysis. The results show that the limits of thermal resistance of heat conduction of the top and side wall envelopes of the energy-saving reactors in Harbin, Shenyang and Beijing under the outdoor temperature in winter were determined. When using other types of reactor materials, such as reinforced concrete, lipo tank, enamel assembly tank, and the insulation materials such as: foam perlite, polyurethane, etc, the thickness of insulation material can be converted according to the heat conduction and thermal resistance of the enclosure structure. Third, according to the method of exergy analysis, the heating system of medium temperature anaerobic fermentation reactor is analyzed and level analysis is used. Exergic losses caused by irreversible process should be reduced as much as possible. The calculation results determine that the inlet and outlet temperatures of the thermal medium of heating system are 45 and 38 ℃respectively, and the heating system efficiency is 86%, and the logarithmic mean temperature difference is 5.8 ℃. The model calculation results showed that the energy level difference between the energy supply and the energy consumption of the reactor is 0.018, which indicates that the energy levels can be matched and energy can be used efficiently. The conclusion can be used as a reference for energy saving design of low energy consumption anaerobic fermentation reactor in cold region.

       

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