Heat recovery from a spray dryer using a glass tube heat exchanger

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Abstract

This project at ABM Chemicals demonstrates the use of a glass tube heat exchanger to recover heat directly from a spray dryer exhaust to pre-heat the inlet air. It was originally envisaged that this would reduce the energy consumption of the dryer by around 20%.

Funding was granted by the Energy Efficiency Office of the Department of Energy under the Energy Efficiency Demonstration Scheme for both a feasibility study and the installation and monitoring of the project. The heat recovery was installed in June 1983 and an initial monitoring exercise carried out. Technical problems have prevented further monitoring and this interim report discusses the background to the project and the results to date.

Because of the corrosive and fouling nature of the exhaust and the arrangement of the ductwork, the most cost-effective option for this particular installation, was a glass tube air-to-air heat exchanger. Depending upon the production outputs, the expected savings were in the range 3.6–5.5 TJ/yr. These savings are worth £10,700 to £16,300/yr from reduced gas consumption and give a simple payback against the £27,000 installation cost, of between 1.7 and 2.5 yr. In other situations it might also be possible to reduce installation costs, which would also lead to a payback of less than two years.

Measurement of the performance of the heat exchanger showed that the amount of heat being recovered, 3.0 TJ/yr, was less than anticipated. Under these conditions the savings would give a 3 yr payback. This reduced performance is believed to be due to a higher-than-anticipated level of fines in the exhaust. This has led to fouling of the heat transfer surfaces, and eventually to the failure of a number of the glass tubes. Measures are currently in hand to reduce the carryover and further monitoring of the replacement exchanger is planned.

This project is one of a package of demonstrations for heat recovery in spray dryers. A similar project at Clayton Aniline uses a run-around coil heat exchanger to recover energy from the dryer exhaust, and a project at BIP Chemicals demonstrates the use of a separate heat source to pre-heat the dryer inlet air.

Within the U.K., widespread adoption of heat recovery on spray dryers would lead to energy savings of 100,000 tonnes of coal equivalent/yr (tce/yr). It is estimated that within the next 5 yr around 20% of

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使用玻璃管换热器从喷雾干燥器中回收热量
ABM Chemicals的这个项目演示了使用玻璃管换热器直接从喷雾干燥器排气中回收热量,以预热进气。最初设想这将使干燥机的能耗减少约20%。能源部能源效率办公室根据能源效率示范计划提供了资金,用于可行性研究以及该项目的安装和监测。热回收装置于1983年6月安装,并进行了初步监测。技术问题阻碍了进一步的监测,本中期报告讨论了该项目的背景和迄今为止的结果。由于排气的腐蚀性和污垢性以及管道系统的布置,这种特殊安装最具成本效益的选择是玻璃管空气对空气热交换器。根据生产产量,预计节省量在3.6–5.5 TJ/yr之间。通过减少天然气消耗,每年可节省10700至16300英镑,相对于1.7至2.5年的27000英镑安装成本,可获得简单的回报。在其他情况下,还可以降低安装成本,这也将导致不到两年的回报。对热交换器性能的测量表明,回收的热量为3.0 TJ/yr,低于预期。在这种情况下,节省下来的资金将有3年的回报期。这种性能下降被认为是由于排气中的细粒度高于预期水平。这导致了传热表面的结垢,并最终导致许多玻璃管失效。目前正在采取措施减少结垢,并计划对更换的交换器进行进一步监测。该项目是喷雾干燥器热回收示范项目之一。Clayton Aniline的一个类似项目使用绕管式换热器从干燥器排气中回收能量,BIP Chemicals的一个项目演示了使用单独的热源来预热干燥器入口空气。在英国,在喷雾干燥器上广泛采用热回收将导致每年节能100000吨煤当量(tce/年)。据估计,在未来5年内
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