Thermal and Environmental Engineering Institute, School of Mechanical Engineering, Tongji University, 1239 Siping Road, Shanghai 200092, China.
Thermal and Environmental Engineering Institute, School of Mechanical Engineering, Tongji University, 1239 Siping Road, Shanghai 200092, China.
Waste Manag. 2020 Apr 1;106:77-87. doi: 10.1016/j.wasman.2020.03.012. Epub 2020 Mar 18.
A technology of sewage sludge (SS) pyrolysis coupled with self-supplied steam reforming of the volatile is developed to utilize the latent heat of the steam vapor released in the SS drying & pyrolysis process. An integrated reactor consisting of a vertical free-falling pyrolysis section and a horizontal screw-moved reforming section is designed for this purpose. The performance of the reactor shows that by changing the moving speed of the char in the reforming section, high quality syngas with an H/CO ratio of 4.37 and a percentage of H + CO up to 66.58 vol% can be obtained at approximately 570-600 °C for the dry SS. There is an optimum moving speed of the screw for producing the highest volume of the syngas. A higher moving speed of the screw also results in a higher concentration of the aromatic compounds in the final pyrolysis oil. When the initial moisture content of SS increases from 0 to 65.50%, the H/CO ratio and H/CO ratio in the syngas increase from 4.37 to 30.87 and from 2.1 to 2.6 correspondingly, and the final oil yield decreases from 24.03 wt% to 14.16 wt%. Moreover, the total energy recovery efficiency decreases from 88.85% to 61.92%, while the energy portion of syngas shows a peak of 44.18% of the total energy input when the initial moisture content is 41.26%. The integrated reactor also provides a good opportunity for adding a catalyst such as dolomite to make the process more effective. The technology developed in this paper provides an approach to deal with SS with a relatively high moisture content.
开发了一种污水污泥 (SS) 热解与挥发性自供蒸汽重整相结合的技术,以利用 SS 干燥和热解过程中释放的蒸汽潜热。为此设计了一个由垂直自由下落热解段和水平螺旋移动重整段组成的集成反应器。该反应器的性能表明,通过改变重整段中焦的移动速度,在约 570-600°C 的温度下,可获得 H/CO 比为 4.37、H+CO 百分比高达 66.58 vol%的高质量合成气,对于干燥的 SS。对于产生最大量合成气,螺杆的最佳移动速度存在。螺杆的移动速度较高,最终热解油中芳香族化合物的浓度也较高。当 SS 的初始水分含量从 0 增加到 65.50%时,合成气中的 H/CO 比和 H/CO 比从 4.37 增加到 30.87 和从 2.1 增加到 2.6,最终油收率从 24.03 wt%降低到 14.16 wt%。此外,总能量回收效率从 88.85%降低到 61.92%,而当初始水分含量为 41.26%时,合成气的能量部分达到总能量输入的 44.18%峰值。该集成反应器还为添加白云石等催化剂提供了一个很好的机会,使工艺更有效。本文开发的技术为处理高水分含量的 SS 提供了一种方法。