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Assessment of Heat Exchangers for the Integration of Concentrated Solar Energy into the Catalytic Hydrothermal Gasification of Biomass

机译:散热器对浓度太阳能集成到生物质催化水热气化的热交换器中的评估

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Abstract >Using concentrated solar energy to power a hydrothermal gasification (HTG) of biomass requires thermal energy storage (TES) to compensate for the inherent intermittence of solar irradiation. The energy transfer from the TES to the HTG process is accomplished through a heat‐transfer fluid (HTF) passing through a heat exchanger (HX) incorporated into the salt‐separation step of the HTG process. The HX performance determines the temperature profile inside the salt separator, thereby influencing the removal of the salts from the feedstock. In this work, we compare the performances of three HX types based on exploiting fluidized beds, porous media, and axially finned tubes. The effect of the HX configuration on the temperature profile inside the salt separator is assessed through CFD simulations considering pure water as the model feed to the separator. We find that all considered HX types could provide the desired temperature profile within the separator. However, the estimate for the power required to pump the HTF through the fluidized‐bed HX is roughly two orders of magnitude higher than those for the axially finned tubular and porous‐media HXs. </abstract> </span> <span class="z_kbtn z_kbtnclass hoverxs" style="display: none;">展开▼</span> </div> <div class="translation abstracttxt"> <span class="zhankaihshouqi fivelineshidden" id="abstract"> <span>机译:</span><abstract xmlns =“http://www.wiley.com/namespaces/wiley”type =“main”xml:lang =“en”> <title type =“main”>抽象</ title> >使用集中用于为生物质的水热气化(HTG)供电的太阳能需要热能存储(TES)以补偿太阳照射的固有间歇性。通过通过通过掺入HTG工艺的盐分离步骤的热交换流体(HTF)来实现来自TES至HTG工艺的能量转移。 HX性能决定了盐分离器内的温度曲线,从而影响来自原料的盐的除去。在这项工作中,我们基于利用流化床,多孔介质和轴向翅片管比较三种HX类型的性能。通过考虑纯水作为模型进料,通过CFD模拟评估HX构型对盐分离器内的温度曲线的影响。我们发现所有考虑的HX类型都可以在隔板内提供所需的温度曲线。然而,通过流化床HX泵送HTF所需的功率的估计大约比轴向翅片管和多孔介质HXS高的两个数量级。</ p> </摘要> </span> <span class="z_kbtn z_kbtnclass hoverxs" style="display: none;">展开▼</span> </div> </div> <div class="record"> <h2 class="all_title" id="enpatent33" >著录项</h2> <ul> <li> <span class="lefttit">来源</span> <div style="width: 86%;vertical-align: text-top;display: inline-block;"> <a href='/journal-foreign-22585/'>《Energy Technology: Generation,Conversion,Storage,Distribution》</a> <b style="margin: 0 2px;">|</b><span>2017年第11期</span><b style="margin: 0 2px;">|</b><span>共14页</span> </div> </li> <li> <div class="author"> <span class="lefttit">作者</span> <p id="fAuthorthree" class="threelineshidden zhankaihshouqi"> <a href="/search.html?doctypes=4_5_6_1-0_4-0_1_2_3_7_9&sertext=Viereck Sebastian&option=202" target="_blank" rel="nofollow">Viereck Sebastian;</a> <a href="/search.html?doctypes=4_5_6_1-0_4-0_1_2_3_7_9&sertext=Keller Jonas&option=202" target="_blank" rel="nofollow">Keller Jonas;</a> <a href="/search.html?doctypes=4_5_6_1-0_4-0_1_2_3_7_9&sertext=Haselbacher Andreas&option=202" target="_blank" rel="nofollow">Haselbacher Andreas;</a> <a href="/search.html?doctypes=4_5_6_1-0_4-0_1_2_3_7_9&sertext=Jovanovic Zoran R.&option=202" target="_blank" rel="nofollow">Jovanovic Zoran R.;</a> <a href="/search.html?doctypes=4_5_6_1-0_4-0_1_2_3_7_9&sertext=Steinfeld Aldo&option=202" target="_blank" rel="nofollow">Steinfeld Aldo;</a> </p> <span class="z_kbtnclass z_kbtnclassall hoverxs" id="zkzz" style="display: none;">展开▼</span> </div> </li> <li> <div style="display: flex;"> <span class="lefttit">作者单位</span> <div style="position: relative;margin-left: 3px;max-width: 639px;"> <div class="threelineshidden zhankaihshouqi" id="fOrgthree"> <p>Solar Technology LaboratoryPaul Scherrer Institute Villigen PSIVilligen 5232 Switzerland;</p> <p>Department of Mechanical and Process EngineeringETH ZürichSonneggstrasse 3 Zurich 8092 Switzerland;</p> <p>Department of Mechanical and Process EngineeringETH ZürichSonneggstrasse 3 Zurich 8092 Switzerland;</p> <p>Department of Mechanical and Process EngineeringETH ZürichSonneggstrasse 3 Zurich 8092 Switzerland;</p> <p>Department of Mechanical and Process EngineeringETH ZürichSonneggstrasse 3 Zurich 8092 Switzerland;</p> </div> <span class="z_kbtnclass z_kbtnclassall hoverxs" id="zhdw" style="display: none;">展开▼</span> </div> </div> </li> <li > <span class="lefttit">收录信息</span> <span style="width: 86%;vertical-align: text-top;display: inline-block;"></span> </li> <li> <span class="lefttit">原文格式</span> <span>PDF</span> </li> <li> <span class="lefttit">正文语种</span> <span>eng</span> </li> <li> <span class="lefttit">中图分类</span> <span><a href="https://www.zhangqiaokeyan.com/clc/233.html" title="能源与动力工程">能源与动力工程;</a></span> </li> <li class="antistop"> <span class="lefttit">关键词</span> <p style="width: 86%;vertical-align: text-top;"> <a style="color: #3E7FEB;" href="/search.html?doctypes=4_5_6_1-0_4-0_1_2_3_7_9&sertext=biomass&option=203" rel="nofollow">biomass;</a> <a style="color: #3E7FEB;" href="/search.html?doctypes=4_5_6_1-0_4-0_1_2_3_7_9&sertext=computational fluid dynamics&option=203" rel="nofollow">computational fluid dynamics;</a> <a style="color: #3E7FEB;" href="/search.html?doctypes=4_5_6_1-0_4-0_1_2_3_7_9&sertext=concentrated solar power&option=203" rel="nofollow">concentrated solar power;</a> <a style="color: #3E7FEB;" href="/search.html?doctypes=4_5_6_1-0_4-0_1_2_3_7_9&sertext=gasification&option=203" rel="nofollow">gasification;</a> <a style="color: #3E7FEB;" href="/search.html?doctypes=4_5_6_1-0_4-0_1_2_3_7_9&sertext=heat exchanger&option=203" rel="nofollow">heat exchanger;</a> </p> <div class="translation"> 机译:生物质;计算流体动力学;集中的太阳能;气化;换热器; </div> </li> </ul> </div> </div> <div class="literature cardcommon"> <div class="similarity "> <h3 class="all_title" id="enpatent66">相似文献</h3> <div class="similaritytab clearfix"> <ul> <li class="active" >外文文献</li> <li >中文文献</li> <li >专利</li> </ul> </div> <div class="similarity_details"> <ul > <li> <div> <b>1. </b><a class="enjiyixqcontent" href="/journal-foreign-detail/0704023183675.html">Assessment of Heat Exchangers for the Integration of Concentrated Solar Energy into the Catalytic Hydrothermal 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Ozonoh&option=202" target="_blank" rel="nofollow" class="tuijian_auth tuijian_authcolor">M. Ozonoh,</a> <a href="/search.html?doctypes=4_5_6_1-0_4-0_1_2_3_7_9&sertext=T.C. Aniokete&option=202" target="_blank" rel="nofollow" class="tuijian_auth tuijian_authcolor">T.C. Aniokete,</a> <a href="/search.html?doctypes=4_5_6_1-0_4-0_1_2_3_7_9&sertext=B.O. Oboirien&option=202" target="_blank" rel="nofollow" class="tuijian_auth tuijian_authcolor">B.O. Oboirien,</a> <span>2018</span> </span> </div> <p class="zwjiyix translation" style="max-width: initial;height: auto;word-break: break-all;white-space: initial;text-overflow: initial;overflow: initial;"> <span>机译:评估5MW CHP共气化厂使用南非煤炭生物质和废轮胎的环境经济和能源参数的数据集</span> </p> </li> <li> <div> <b>7. </b><a class="enjiyixqcontent" href="/open-access_resources_thesis/010006793629.html ">This article presents a new numerical model describing the behaviour of a thermally thick wood sample exposed to high solar heat flux (above 1 MW/m2). A preliminary study based on dimensionless numbers is used to classify the problem and support model building assumptions. Then, a model based on mass, momentum and energy balance equations is proposed. These equations are coupled with liquid-vapour drying model and pseudo species biomass degradation model. By comparing to a former experimental study, preliminary results have shown that these equations are not enough to accurately predict biomass behaviour under high solar heat flux. Indeed, a char layer acting as radiative shield forms on the sample exposed surface. In addition to this classical set of equations, it is mandatory to take into account radiation penetration into the medium. Furthermore, as biomass contains water, medium deformation consecutively to char steam gasification must also be implemented. Finally, with the addition of these two strategies, the model is able to properly capture the degradation of biomass when exposed to high radiative heat flux over a range of sample initial moisture content. Additional insights of biomass behaviour under high solar heat flux were also derived. Drying, pyrolysis and gasification fronts are present at the same time inside of the sample. The coexistence of these three thermochemical fronts leads to char gasification by the steam produced from drying of the sample, which it is the main phenomenon behind medium ablation.</a> <b>[O] </b> . <span> <a href="/search.html?doctypes=4_5_6_1-0_4-0_1_2_3_7_9&sertext=Pozzobon, Victor&option=202" target="_blank" rel="nofollow" class="tuijian_auth tuijian_authcolor">Pozzobon, Victor,</a> <a href="/search.html?doctypes=4_5_6_1-0_4-0_1_2_3_7_9&sertext=Salvador, Sylvain&option=202" target="_blank" rel="nofollow" class="tuijian_auth tuijian_authcolor">Salvador, Sylvain,</a> <a href="/search.html?doctypes=4_5_6_1-0_4-0_1_2_3_7_9&sertext=Bézian, Jean Jacques&option=202" target="_blank" rel="nofollow" class="tuijian_auth tuijian_authcolor">Bézian, Jean Jacques </a> <span>2018</span> </span> </div> <p class="zwjiyix translation" style="max-width: initial;height: auto;word-break: break-all;white-space: initial;text-overflow: initial;overflow: initial;"> <span>机译:本文提供了一个新的数值模型,该模型描述了暴露于高太阳热通量(高于1 / MW / m2)的热厚木材样品的行为。基于无量纲数的初步研究用于对问题进行分类并支持模型构建假设。然后,提出了一种基于质量,动量和能量平衡方程的模型。这些方程式与液体蒸汽干燥模型和假物种生物质降解模型耦合。通过与以前的实验研究进行比较,初步结果表明,这些方程不足以准确预测高太阳热通量下的生物量行为。的确,在样品暴露的表面上形成了充当辐射屏蔽层的炭层。除了这套经典的方程式之外,还必须考虑到辐射向介质的渗透。此外,由于生物质中含有水,因此还必须在炭蒸气汽化后进行连续的介质变形。最后,通过添加这两种策略,该模型能够在一定范围的样品初始水分含量下暴露于高辐射热通量的情况下,正确捕获生物质的降解。还得出了在高太阳热通量下生物量行为的其他见解。样品内部同时存在干燥,热解和气化前沿。这三个热化学前沿的共存会导致样品干燥产生的蒸汽产生焦炭气化,这是介质烧蚀的主要现象。</span> </p> </li> </ul> <ul style="display: none;"> <li> <div> <b>1. </b><a class="enjiyixqcontent" href="/academic-journal-cn_huadian-technology_thesis/0201290781196.html">Fe基催化剂在生物质催化气化中制富氢气体的应用</a> <b>[J]</b> <span> <a href="/search.html?doctypes=4_5_6_1-0_4-0_1_2_3_7_9&sertext=周瑜枫&option=202" target="_blank" rel="nofollow" class="tuijian_auth tuijian_authcolor"> . 周瑜枫</a> <a href="/search.html?doctypes=4_5_6_1-0_4-0_1_2_3_7_9&sertext=王学涛&option=202" target="_blank" rel="nofollow" class="tuijian_auth tuijian_authcolor">,王学涛</a> <a 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