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CN115945143A - A fluidized bed reactor for solar fuel production - Google Patents

A fluidized bed reactor for solar fuel production Download PDF

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CN115945143A
CN115945143A CN202211183862.3A CN202211183862A CN115945143A CN 115945143 A CN115945143 A CN 115945143A CN 202211183862 A CN202211183862 A CN 202211183862A CN 115945143 A CN115945143 A CN 115945143A
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fluidized bed
section
solar
fuel production
riser
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毛颖
陈巨辉
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Harbin University of Science and Technology
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Harbin University of Science and Technology
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Abstract

本发明涉及热化学储能聚光太阳能发电和流化床领域,特别是一种太阳能燃料生产的流化床反应器,由两个同心圆管组成,连接在具有锥形几何形状的截面上,在干舷区,由于截面的增加,气体速度逐渐降低,固体颗粒沿着圆锥段的壁面下降,最终被输送至环隙段,颗粒通过重力作用流向环空部分的底部,直到通过在提升管中钻的四个小孔再次进入提升管,在提升管的出口,流化的颗粒直接与集中的太阳辐射相互作用来提高其温度,并促进用于热化学储能和太阳能燃料生产的吸热化学反应过程。

Figure 202211183862

The present invention relates to the fields of thermochemical energy storage concentrating solar power generation and fluidized bed, especially a fluidized bed reactor for solar fuel production, which consists of two concentric circular tubes connected on a section with a conical geometry, In the freeboard area, due to the increase of the section, the gas velocity gradually decreases, and the solid particles descend along the wall of the conical section, and are finally transported to the annulus section. The particles flow to the bottom of the annulus by gravity until they pass through the riser. The four small holes drilled again enter the riser, where the fluidized particles interact directly with the concentrated solar radiation to increase their temperature and promote endothermic chemistry for thermochemical energy storage and solar fuel production. reaction process.

Figure 202211183862

Description

一种太阳能燃料生产的流化床反应器A fluidized bed reactor for solar fuel production

技术领域technical field

本发明涉及热化学储能聚光太阳能发电和流化床领域,具体涉及一种太阳能燃料生产的流化床反应器。The invention relates to the field of thermochemical energy storage concentrated solar power generation and fluidized bed, in particular to a fluidized bed reactor for solar fuel production.

背景技术Background technique

由于太阳能具有间歇性、低密度和不稳定性、难以持续供应的缺点,纯太阳能热发电的广泛应用目前仍有许多问题需要解决,其中如何实现太阳能高效、大规模的储存,保证持续稳定供给是太阳能热发电技术的关键,将太阳能储存在太阳能热化学燃料中具有能量转换效率高、存储和运输方便等优点,太阳能的热化学储能允许实现更大的密度和几乎无限的时间尺度的能量存储和可调度性,而流化床反应器可以改善太阳光在催化剂床上分布不均匀以及提高反应物与催化剂的接触面积问题,减小反应器的温度波动性,提高温度分布的均匀性,但是太阳能燃料生产的流化床反应器应用还不是很广泛,对于热量转换中辐射热的利用率还不够充分。Due to the intermittent, low density and instability of solar energy, which makes it difficult to supply continuously, there are still many problems to be solved for the wide application of pure solar thermal power generation. Among them, how to realize efficient and large-scale storage of solar energy and ensure continuous and stable supply is a key issue. The key to solar thermal power generation technology, storing solar energy in solar thermochemical fuels has the advantages of high energy conversion efficiency, convenient storage and transportation, and thermal chemical energy storage of solar energy allows for greater density and almost unlimited time scales. and schedulability, while the fluidized bed reactor can improve the uneven distribution of sunlight on the catalyst bed and increase the contact area between the reactant and the catalyst, reduce the temperature fluctuation of the reactor, and improve the uniformity of the temperature distribution, but the solar energy Fluidized bed reactors for fuel production are not widely used, and the utilization rate of radiant heat in heat conversion is not enough.

发明内容Contents of the invention

本发明为了最大限度地收集太阳能,承受典型的高温聚光太阳能热发电系统的高浓缩通量,并确保反应材料的温度分布均匀,提供了一种新型的用于太阳能热发电和太阳能燃料生产的流化床反应器。In order to maximize the collection of solar energy, withstand the high concentration flux of typical high-temperature concentrating solar thermal power generation systems, and ensure uniform temperature distribution of reaction materials, the present invention provides a new type of solar thermal power generation and solar fuel production Fluidized bed reactor.

本发明的技术方案是:一种太阳能燃料生产的流化床反应器,包括内管、外管、孔、锥形部分和石英窗口,内管和外管同心装配,上部与内角夹角为30°,高度为120mm的锥形部分相连,锥形部分的顶部由一个透明的3mm厚,在250~2500μm波长范围内透射率为90%的石英窗口封闭,使太阳辐射进入保持密封的反应堆运行,气体出口位于锥形部分的上部,在距底部40mm高度的内管侧表面钻了四个直径为6mm的等距孔,所有的反应堆组件都由不锈钢制成,反应器采用多层岩棉毯进行隔热,以尽量减少对外界环境的热损失。The technical scheme of the present invention is: a fluidized bed reactor for solar fuel production, including an inner tube, an outer tube, a hole, a tapered part and a quartz window, the inner tube and the outer tube are assembled concentrically, and the angle between the upper part and the inner angle is 30° °, the conical part with a height of 120mm is connected, and the top of the conical part is closed by a transparent 3mm thick quartz window with a transmittance of 90% in the wavelength range of 250-2500μm, allowing solar radiation to enter the sealed reactor operation, The gas outlet is located on the upper part of the conical part, and four equidistant holes with a diameter of 6 mm are drilled on the side surface of the inner tube at a height of 40 mm from the bottom. All reactor components are made of stainless steel, and the reactor is covered with multi-layer rock wool blankets. Insulated to minimize heat loss to the outside environment.

本发明与现有技术相比具有以下有益效果:在提升管的出口,流化的颗粒直接与集中的太阳辐射相互作用来提高其温度,并促进用于热化学储能和太阳能燃料生产的吸热化学反应过程,在干舷区,由于截面的增加,气体速度逐渐降低,固体颗粒沿着圆锥段的壁面下降,最终被输送至环隙段,在这里,颗粒通过重力作用流向环空部分的底部,直到通过在提升管中钻的四个小孔再次进入提升管,从传热学的角度来看,提升管和环隙段可以被认为是一个双管换热器,其中床层固体在提升管中向上运动时,通过在环隙段运动的热颗粒进行预热,而在干舷段则通过集中的太阳辐射进行加热,通过双管换热器回收出干燥器部分的固体流的显热,以预热进入提升管的床固体流。The present invention has the following beneficial effects over the prior art: at the outlet of the riser, the fluidized particles interact directly with the concentrated solar radiation to increase their temperature and facilitate absorption for thermochemical energy storage and solar fuel production. During the thermochemical reaction process, in the freeboard area, due to the increase of the cross section, the gas velocity gradually decreases, and the solid particles descend along the wall of the conical section, and are finally transported to the annulus section, where the particles flow to the annulus by gravity. bottom, until it enters the riser again through four small holes drilled in the riser, From a heat transfer point of view, the riser and annulus section can be considered as a double tube heat exchanger where the bed solids are in Preheated by hot particles moving in the annulus section and heated by concentrated solar radiation in the freeboard section as it moves upwards in the riser, the apparent solids flow in the dryer section is recovered through a double-pipe heat exchanger. heat to preheat the bed solids stream entering the riser.

附图说明Description of drawings

图1为太阳能燃料生产的流化床反应器结构图。Figure 1 is a structural diagram of a fluidized bed reactor for solar fuel production.

图2为内管与外管结构图。Figure 2 is a structural diagram of the inner tube and the outer tube.

图3为挖孔位置局部放大图。Figure 3 is a partial enlarged view of the digging location.

图中:1内管、2外管、3孔、4锥形部分、5石英窗口。In the figure: 1 inner tube, 2 outer tube, 3 hole, 4 tapered part, 5 quartz window.

具体实施方式Detailed ways

下面将结合本发明例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例,基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below in conjunction with the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only some of the embodiments of the present invention, not all of them. Based on this The embodiments in the invention, and all other embodiments obtained by persons of ordinary skill in the art without creative efforts, all belong to the scope of protection of the present invention.

请参阅图1,一种太阳能燃料生产的流化床反应器,包括内管1、外管2、孔3、锥形部分4和石英窗口5,内管的内径为10mm,外径为12mm,长度为120mm,外管的内径为16mm,外径为21mm,长度为70mm,内管和外管同心装配,标识两个区域,内管内部的区域称为隔水管段,内外管之间的间隙称为环空段,相应地,内管和外管将分别简称为立管和环空。Please refer to Fig. 1, a kind of fluidized bed reactor of solar energy fuel production, comprises inner tube 1, outer tube 2, hole 3, conical part 4 and quartz window 5, and the inner diameter of inner tube is 10mm, and outer diameter is 12mm, The length is 120mm, the inner diameter of the outer pipe is 16mm, the outer diameter is 21mm, and the length is 70mm. The inner pipe and the outer pipe are assembled concentrically, and two areas are marked. The area inside the inner pipe is called the riser section, and the gap between the inner and outer pipes It is called the annulus segment, and accordingly, the inner pipe and the outer pipe will be referred to simply as the riser and the annulus, respectively.

在距底部40mm高度的内管侧表面钻四个直径为6mm的等距孔,以实现流化床反应器内固体从环空到提升管段的循环,当两管装配在一起时,隔水管的顶部相对于环空突出约10mm。Drill four equidistant holes with a diameter of 6mm on the side surface of the inner pipe at a height of 40mm from the bottom to realize the circulation of solids in the fluidized bed reactor from the annulus to the riser section. When the two pipes are assembled together, the riser The top protrudes about 10mm from the annulus.

最后,外径为6mm,内径为4mm的管喷嘴作为流化气体分布器位于提升管底部,环隙上部与内角夹角为30°,高度为120mm的锥形段相连,锥形部分的顶部由一个透明的3mm厚,在250~2500μm波长范围内透射率为90%的石英窗口封闭,使太阳辐射进入保持密封的反应堆运行,气体出口位于锥形部分的上部,所有的反应堆组件都由不锈钢制成,反应器采用多层岩棉毯进行隔热,以尽量减少对外界环境的热损失。Finally, a tube nozzle with an outer diameter of 6mm and an inner diameter of 4mm is located at the bottom of the riser as a fluidizing gas distributor, and the upper part of the annulus is connected to a conical section with an inner angle of 30° and a height of 120mm. The top of the conical section is formed by A transparent 3mm thick quartz window with a transmittance of 90% in the wavelength range of 250-2500μm is closed to allow solar radiation to enter the sealed reactor. The gas outlet is located in the upper part of the cone. All reactor components are made of stainless steel. As a result, the reactor is insulated with multi-layer rock wool blankets to minimize heat loss to the external environment.

所述太阳能燃料生产的流化床反应器通过将流化气体通过管喷嘴送入上升管来调节反应器的流体力学,采用不同的颗粒材料作为惰性床料,由硅砂、莫来石和矾土粉组成,通常,床层固体惰性库存量保持在10~12g左右,使用天然石灰石作为反应材料,石灰石用量约为2~3g。The fluidized bed reactor for solar fuel production adjusts the hydrodynamics of the reactor by sending the fluidization gas through the tube nozzle into the riser, using different granular materials as inert bed materials, consisting of silica sand, mullite and alumina powder Composition, usually, the bed solid inert inventory is kept at about 10-12g, natural limestone is used as the reaction material, and the amount of limestone is about 2-3g.

Claims (2)

1. A fluidized bed reactor for producing solar fuel comprises an inner tube, an outer tube, holes, a conical part and a quartz window, wherein the inner tube and the outer tube are assembled concentrically, the upper part of the inner tube is connected with the conical part, the top of the conical part is closed by the quartz window, and four equidistant holes are drilled on the side surface of the inner tube.
2. A fluidized bed reactor for solar fuel production according to claim 1, characterized by comprising: the included angle of the inner angle of the conical section is 30 degrees, and the height of the conical section is 120mm; four equidistant small holes with the diameter of 6mm are drilled in the riser.
CN202211183862.3A 2022-09-27 2022-09-27 A fluidized bed reactor for solar fuel production Pending CN115945143A (en)

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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017024338A1 (en) * 2015-08-13 2017-02-16 The University Of Adelaide Solar receiver
CN108036522A (en) * 2017-11-08 2018-05-15 哈尔滨理工大学 A kind of internal-circulation type fluid bed-solar energy particle receiver

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017024338A1 (en) * 2015-08-13 2017-02-16 The University Of Adelaide Solar receiver
CN108036522A (en) * 2017-11-08 2018-05-15 哈尔滨理工大学 A kind of internal-circulation type fluid bed-solar energy particle receiver

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
TREGAMBI C ET AL.: ""Directly irradiated fluidized bed reactor for thermochemical energy storage and solar fuels production"", 《POWDER TECHNOLOGY》, vol. 366, 19 February 2020 (2020-02-19), pages 460 - 469, XP086117875, DOI: 10.1016/j.powtec.2020.02.045 *

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Application publication date: 20230411