首页> 外文期刊>Environmental engineering research >Light Tar Decomposition of Product Pyrolysis Gas from Sewage Sludge in a Gliding Arc Plasma Reformer
【24h】

Light Tar Decomposition of Product Pyrolysis Gas from Sewage Sludge in a Gliding Arc Plasma Reformer

机译:滑动电弧等离子体重整器中污水污泥中产物热解气的轻焦油分解

获取原文
获取原文并翻译 | 示例
           

摘要

Pyrolysis/gasification technology utilizes an energy conversion technique from various waste resources, such as biomass, solid waste, sewage sludge, and etc. to generating a syngas (synthesis gas). However, one of the major problems for the pyrolysis gasification is the presence of tar in the product gas. The tar produced might cause damages and operating problems on the facility. In this study, a gliding arc plasma reformer was developed to solve the previously acknowledged issues. An experiment was conducted using surrogate benzene and naphthalene, which are generated during the pyrolysis and/or gasification, as the representative tar substance. To identify the characteristics of the influential parameters of tar decomposition, tests were performed on the steam feed amount (steam/carbon ratio), input discharge power (specific energy input, SEI), total feed gas amount and the input tar concentration. In benzene, the optimal operating conditions of the gliding arc plasma 2 in steam to carbon (S/C) ratio, 0.98 kWh/m~3 in SEI, 14 L/min in total gas feed rate and 3.6% in benzene concentration. In naphthalene, 2.5 in S/C ratio, 1 kWh/m3 in SEI, 18.4 L/min in total gas feed rate and 1% in naphthalene concentration. The benzene decomposition efficiency was 95%, and the energy efficiency was 120 g/kWh. The naphthalene decomposition efficiency was 79%, and the energy yield was 68 g/kWh.
机译:热解/气化技术利用了来自各种废物资源的能量转换技术,例如生物质,固体废物,污水污泥等,以产生合成气(合成气)。然而,热解气化的主要问题之一是在产物气中存在焦油。产生的焦油可能会造成设施损坏和运行问题。在这项研究中,开发了一种滑动电弧等离子体重整器,以解决先前公认的问题。使用在热解和/或气化过程中产生的替代苯和萘作为代表焦油物质进行了实验。为了确定焦油分解影响参数的特征,对蒸汽进料量(蒸汽/碳比),输入排出功率(比能量输入,SEI),总进料气量和输入焦油浓度进行了测试。在苯中,滑移电弧等离子体2的最佳运行条件为:蒸汽与碳(S / C)比,SEI为0.98 kWh / m〜3,总气体进料速度为14 L / min和苯浓度为3.6%。在萘中,S / C比为2.5,SEI为1 kWh / m3,总气体进料速度为18.4 L / min,萘浓度为1%。苯的分解效率为95%,能量效率为120 g / kWh。萘的分解效率为79%,能量产率为68g / kWh。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号