CN102078782A - Method and device for improving internal particle circulation in lift pipe through return air at tower top - Google Patents
Method and device for improving internal particle circulation in lift pipe through return air at tower top Download PDFInfo
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Abstract
本发明提供的是一种通过塔顶回送风提高提升管内颗粒内循环的装置及方法。装置包括提升管,提升管的顶部为约束结构,提升管的侧壁上设有风机出口,在提升管的顶部侧壁上设有一个与约束结构相通的回送风口,回送风口位于风机出口的上方且回送风口与风机出口位于提升管的同一侧,在提升管内设置有用于回流颗粒下行的管道或隔板。在提升管的顶部的约束结构处水平引入回送风,回送风气流将提升管顶部依靠约束结构分离的颗粒向下携带,经用于回流颗粒下行的管道或隔板送入提升管底部。本发明有效利用了顶部约束结构分离作用,而且提升管系统阻力增加不明显,无明显能耗增加。可应用于化工、粮食干燥、烟气污染物质量领域领域。
The invention provides a device and a method for improving the internal circulation of particles in a riser through the return air at the top of the tower. The device includes a riser, the top of the riser is a restraint structure, the side wall of the riser is provided with a fan outlet, and the top side wall of the riser is provided with a return air outlet connected to the restraint structure, and the return air outlet is located above the fan outlet And the return tuyere and the fan outlet are located on the same side of the riser, and a pipe or partition for the return particles to descend is arranged in the riser. The return air is introduced horizontally at the confinement structure at the top of the riser, and the return air flow will carry the particles separated by the confinement structure at the top of the riser downwards, and send them to the bottom of the riser through the pipe or partition for the return particles to descend. The invention effectively utilizes the separation effect of the top constraint structure, and the resistance of the riser system does not increase significantly, and the energy consumption does not increase significantly. It can be used in the fields of chemical industry, grain drying, and flue gas pollutant quality.
Description
技术领域technical field
本发明涉及的是一种提高提升管内颗粒内循环的方法,具体为一种通过回送风与提升管出口约束结构相结合实现强化颗粒内部循环的方法。本发明也涉及一种能提高提升管内颗粒内循环的提升管。The invention relates to a method for improving the internal circulation of particles in a riser, in particular to a method for enhancing the internal circulation of particles through the combination of return air and the restrictive structure at the outlet of the riser. The invention also relates to a riser that improves the internal circulation of particles in the riser.
背景技术Background technique
气固流态化反应已经成为过程工业反应与分离设备的主流,在工业生产中占有极为重要的地位。世家各大石油化工企业目前普遍采用的是流态化催化裂化装置,以及各大火力发电企业普遍采用大型循环流化床锅炉,循环流化床烟气过六技术、都是流态化技术杰出的应用范例。Gas-solid fluidization reaction has become the mainstream of process industry reaction and separation equipment, and occupies an extremely important position in industrial production. At present, major petrochemical companies in the family generally use fluidized catalytic cracking units, and major thermal power generation companies generally use large-scale circulating fluidized bed boilers. application example.
提升管是流态化反应器的普遍称呼。提高提升管内颗粒的内部循环效果,一直是行业内持续研发的课题。以往的措施多是采用增加内部构件、改变塔体结构实现的,这些方法多数存在磨损、不适合含湿量高、粘性大的物料等问题。颗粒的内循环强化技术,一直是多相流技术领域研究的热点和难点问题。现有的提升管在使用时,在约束结构的作用下沿塔体壁面回落入塔内的颗粒,在塔体内的下行深度有限,很快就又被向上流动的气流带到塔顶,循环效果较差。因此说,现有的提升管在使用时存在颗粒在提升管内停留时间短、造成提升管颗粒的内部循环效果较差,为了延长颗粒在提升管内停留时间不得不加长提升管的有效工作长度,使提升管的工作体积增大,造成不必要的浪费等问题。Riser is a common name for a fluidized reactor. Improving the internal circulation effect of particles in the riser has always been a subject of continuous research and development in the industry. Most of the previous measures were achieved by adding internal components and changing the structure of the tower body. Most of these methods have problems such as wear and tear, and are not suitable for materials with high moisture content and high viscosity. The internal circulation enhancement technology of particles has always been a hot and difficult issue in the field of multiphase flow technology research. When the existing riser is in use, the particles that fall back into the tower along the wall of the tower body under the action of the restraint structure have a limited downward depth in the tower body, and are quickly brought to the top of the tower by the upward-flowing airflow, and the circulation effect poor. Therefore, when the existing riser is in use, there is a short residence time of the particles in the riser, which causes the internal circulation effect of the particles in the riser to be poor. In order to prolong the residence time of the particles in the riser, the effective working length of the riser has to be lengthened, so that The working volume of the riser increases, causing problems such as unnecessary waste.
发明内容Contents of the invention
本发明的目的在于提供一种能延长颗粒在提升管内停留时间、改善提升管内颗粒的内部循环效果的通过塔顶回送风提高提升管内颗粒内循环的装置及方法。The object of the present invention is to provide a device and method for improving the internal circulation of particles in the riser through the return air at the top of the tower, which can prolong the residence time of particles in the riser and improve the internal circulation effect of the particles in the riser.
本发明的目的是这样实现的:The purpose of the present invention is achieved like this:
本发明的通过塔顶回送风提高提升管内颗粒内循环的装置包括提升管,所述提升管的顶部为约束结构,所述提升管的侧壁上设有风机出口,在提升管的顶部侧壁上设有一个与约束结构相通的回送风口,回送风口位于风机出口的上方且回送风口与风机出口位于提升管的同一侧,在提升管内设置有用于回流颗粒下行的管道或隔板,且所述用于回流颗粒下行的管道或隔板与回送风口相对设置。The device for improving the internal circulation of particles in the riser by returning air from the top of the tower of the present invention comprises a riser, the top of the riser is a restraint structure, the side wall of the riser is provided with a fan outlet, and on the top side of the riser There is a return air outlet connected to the restraint structure on the wall, the return air outlet is located above the fan outlet and the return air outlet and the fan outlet are located on the same side of the riser, and a pipe or partition for the return particles to descend is arranged in the riser, and the The above-mentioned pipes or partitions for the downward flow of the return particles are arranged opposite to the return air outlet.
本发明的通过塔顶回送风提高提升管内颗粒内循环的方法,选用的通过塔顶回送风提高提升管内颗粒内循环的装置包括提升管,提升管的顶部为约束结构,提升管的侧壁上设有风机出口,在提升管的顶部侧壁上设有一个与约束结构相通的回送风口,回送风口位于风机出口的上方且回送风口与风机出口位于提升管的同一侧,在提升管内设置有用于回流颗粒下行的管道或隔板,且所述用于回流颗粒下行的管道或隔板与回送风口相对设置;在提升管的顶部的约束结构处水平引入回送风,回送风气流将提升管顶部依靠约束结构分离的颗粒向下携带,经用于回流颗粒下行的管道或隔板送入提升管底部。According to the method for increasing the internal circulation of particles in the riser through the return air at the top of the tower, the selected device for improving the internal circulation of the particles in the riser through the return air at the top of the tower includes a riser, the top of the riser is a restraint structure, and the side of the riser There is a fan outlet on the wall, and a return air outlet connected to the restraint structure is provided on the top side wall of the riser. The return air outlet is located above the fan outlet and the return air outlet and the fan outlet are located on the same side of the riser. There are pipes or partitions for the downward flow of the return particles, and the pipes or partitions for the downward flow of the return particles are arranged opposite to the return air outlet; the return air is introduced horizontally at the restraint structure at the top of the riser, and the return air flow will The top of the riser is carried downward by the particles separated by the confinement structure, and sent to the bottom of the riser through the pipe or partition used for the downflow of the particles.
所述水平引入回送风是将提升管系统风机出口气体引送到提升管顶部。Said horizontal introduction of return air is to lead the outlet gas of the fan of the riser system to the top of the riser.
所述水平引入回送风是采用一小型风机或直接利用现场气力输送高压空气提供风源。The horizontally introduced return air is provided by a small blower fan or directly using on-site pneumatically conveyed high-pressure air.
最好控制回送风的风速为10-15m/s。It is best to control the wind speed of the return air to 10-15m/s.
本发明解决了现有的提升管在使用时存在颗粒在提升管内停留时间短、造成提升管颗粒的内部循环效果较差以及为了延长颗粒在提升管内停留时间不得不增加提升管的高度等问题。The present invention solves the problems that the particles stay in the riser for a short time when the existing riser is in use, the internal circulation effect of the particles in the riser is poor, and the height of the riser has to be increased in order to prolong the residence time of the particles in the riser.
本发明的技术要点为:将提升管反应器系统风机出口气体部分引入回送到提升管出口顶部;在提升管出口相反侧设置下行流通通道;依靠提升管顶部约束结构的气固分离作用和回送风的气力输送作用将顶部颗粒回送到提升管下部,实现了提升管内颗粒的强化内部循环。The technical points of the present invention are as follows: the gas part of the fan outlet of the riser reactor system is introduced back to the top of the riser outlet; a downward circulation channel is arranged on the opposite side of the riser outlet; the gas-solid separation and return is carried out by means of the restraint structure at the top of the riser The pneumatic conveying action of the wind returns the top particles to the lower part of the riser, achieving an enhanced internal circulation of the particles in the riser.
本发明的有益效果是:The beneficial effects of the present invention are:
本发明方法利用回送风以及在在提升管出口相反侧设置下行流通通道的方式来提高提升管内颗粒内循环效果,依靠提升管顶部约束结构的气固分离作用和回送风的气力输送作用将顶部颗粒回送到提升管下部,实现了提升管内颗粒的强化内部循环。本方法可以增加提升管内颗粒浓度5-10%,增加了颗粒停留时间(相当于降低了提升管的高度),进而增强提升管颗粒的内部循环效果。在相同反应参数条件下,可适当降低提升管的高度。降低提升管的高度,等于降低了设备投资费用,同时由于气体流程的缩短,可以明显降低系统流动阻力,进而实现运行电耗的节约。仅以10m/s的气体流速计算,每降低提升管高度1米,约可节约实现10Pa所有的阻力损失,运行节能比例约0.03%The method of the present invention utilizes the return air and arranges the downward circulation channel on the opposite side of the riser outlet to improve the internal circulation effect of the particles in the riser, relying on the gas-solid separation effect of the restraint structure on the top of the riser and the pneumatic conveying effect of the return air. The top pellets are fed back to the lower portion of the riser, enabling enhanced internal circulation of the pellets in the riser. The method can increase the particle concentration in the riser by 5-10%, increases the particle residence time (equivalent to reducing the height of the riser), and then enhances the internal circulation effect of the riser particles. Under the same reaction parameter conditions, the height of the riser can be appropriately reduced. Reducing the height of the riser is equivalent to reducing the equipment investment cost. At the same time, due to the shortening of the gas flow, the flow resistance of the system can be significantly reduced, thereby realizing the saving of operating power consumption. Calculated only at a gas flow rate of 10m/s, every time the height of the riser is reduced by 1 meter, all resistance losses of 10Pa can be saved, and the energy saving ratio of operation is about 0.03%.
本发明通过风送颗粒实现颗粒的强化内部循环,可以适应于一定含湿量的颗粒实现稳定循环;本发明有效利用了顶部约束结构分离作用,而且提升管系统阻力增加不明显,无明显能耗增加。本发明可应用于化工、粮食干燥、烟气污染物质量领域领域。The invention realizes the enhanced internal circulation of the particles by blowing the particles by air, and can be adapted to achieve stable circulation of the particles with a certain moisture content; the invention effectively utilizes the separation effect of the top constraint structure, and the resistance of the riser system does not increase significantly, and there is no obvious energy consumption Increase. The invention can be applied to the fields of chemical industry, grain drying and flue gas pollutant quality.
附图说明Description of drawings
图1是提升管的原理示意图;Figure 1 is a schematic diagram of the principle of the riser;
图2是图1的A-A剖视图(塔体顶部约束结构内颗粒相流动示意图);Fig. 2 is the A-A sectional view of Fig. 1 (the schematic diagram of particle phase flow in the confinement structure at the top of the tower body);
图3是本发明的通过塔顶回送风提高提升管内颗粒内循环的装置的结构及其工作原理示意图。Fig. 3 is a schematic diagram of the structure and working principle of the device for improving the internal circulation of particles in the riser by returning air from the top of the tower according to the present invention.
具体实施方式Detailed ways
下面结合附图举例对本发明做更详细的描述:The present invention is described in more detail below in conjunction with accompanying drawing example:
具体实施方式一:如图3所示,本实施方式所述的通过塔顶回送风提高提升管内颗粒内循环的方法的具体实现过程为:步骤一、在提升管1的顶部的约束结构1-1处水平引入回送风,且回送风与提升管1风机出口1-2同侧,并控制回送风的风速为3-18m/s;步骤二、在提升管1内设置一个用于回流颗粒下行的管道或隔板2;步骤三、利用该回送风气流将提升管1顶部依靠约束结构1-1分离的颗粒向下携带,经用于回流颗粒下行的管道或隔板2送入提升管1底部。Specific embodiment one: as shown in Figure 3, the specific implementation process of the method for improving the internal circulation of particles in the riser through the return air at the top of the tower described in this embodiment is: Step 1, the constraint structure 1 at the top of the riser 1 The return air is introduced horizontally at -1, and the return air is on the same side as the fan outlet 1-2 of the riser 1, and the wind speed of the return air is controlled to be 3-18m/s; The pipeline or
具体实施方式二:本实施方式在步骤一中,水平引入回送风的方式为:将提升管系统风机出口气体引送到提升管顶部。回送风将顶部约束结构颗粒直接吹送至下行结构,可以实现低能耗条件下的颗粒塔内回送。其它组成及连接关系与具体实施方式一相同。Specific implementation mode 2: In step 1 of this implementation mode, the method of horizontally introducing return air is: leading the air from the outlet of the fan of the riser system to the top of the riser. The return air blows the particles of the top confinement structure directly to the downlink structure, which can realize the return in the particle tower under the condition of low energy consumption. Other components and connections are the same as those in the first embodiment.
具体实施方式三:本实施方式在步骤一中,水平引入回送风的方式为:采用一小型风机或直接利用现场气力输送高压空气,提供该风量。回送风将顶部约束结构颗粒直接吹送至下行结构,可以实现低能耗条件下的颗粒塔内回送。其它组成及连接关系与具体实施方式一相同。Specific implementation mode 3: In step 1 of this implementation mode, the method of horizontally introducing return air is: using a small fan or directly using on-site pneumatic power to transport high-pressure air to provide the air volume. The return air blows the particles of the top confinement structure directly to the downlink structure, which can realize the return in the particle tower under the condition of low energy consumption. Other components and connections are the same as those in the first embodiment.
具体实施方式四:如图1所示,本实施方式在步骤一中,控制回送风的风速为5-15m/s。回送风将顶部约束结构颗粒直接吹送至下行结构,可以实现低能耗条件下的颗粒塔内回送。其它组成及连接关系与具体实施方式一相同。Embodiment 4: As shown in FIG. 1 , in step 1 of this embodiment, the wind speed of the return air is controlled to be 5-15 m/s. The return air blows the particles of the top confinement structure directly to the downlink structure, which can realize the return in the particle tower under the condition of low energy consumption. Other components and connections are the same as those in the first embodiment.
具体实施方式五:如图3所示,本实施方式所述的实现上述方法的专用装置包括提升管1,所述提升管1的顶部为约束结构1-1,所述提升管1的侧壁上设有风机出口1-2,在提升管1的顶部侧壁上设有一个与约束结构1-1相通的回送风口1-3,回送风口1-3位于风机出口1-2的上方且回送风口1-3与风机出口1-2位于提升管1的同一侧,在提升管1内设置有用于回流颗粒下行的管道或隔板2,且所述用于回流颗粒下行的管道或隔板2与回送风口1-3相对设置。本发明所述装置结构简单,易于实现。Specific embodiment five: as shown in Figure 3, the special device for realizing the above method described in this embodiment includes a riser 1, the top of the riser 1 is a restraint structure 1-1, and the side wall of the riser 1 There is a fan outlet 1-2 on the top, and a return air outlet 1-3 communicated with the restraint structure 1-1 is provided on the top side wall of the riser 1. The return air outlet 1-3 is located above the fan outlet 1-2 and returns The tuyere 1-3 and the fan outlet 1-2 are located on the same side of the riser 1, and a pipe or
本发明原理分析如下:Principle of the present invention is analyzed as follows:
现有技术中的提升管顶部流动情况如下:气流到顶部出口后沿水平出口流出,部分颗粒继续保持向上运动势头,碰到顶部玻璃板后开始向塔体四壁成花瓣型扩散,如图1,出口侧的颗粒被水平气流带走,其它3面的颗粒沿塔体壁面回落入塔内,但是其下行深度有限,很快就又被带到塔顶。The flow situation at the top of the riser in the prior art is as follows: the air flow flows out along the horizontal outlet after reaching the top outlet, and some particles continue to move upward, and after hitting the top glass plate, they begin to diffuse toward the walls of the tower body in a petal shape, as shown in Figure 1 , the particles on the outlet side are taken away by the horizontal airflow, and the particles on the other three sides fall back into the tower along the wall of the tower body, but their descending depth is limited, and they are quickly brought to the top of the tower.
本发明将提升管系统风机出口气体引送到提升管顶部,(也可增加一小型风机或直接利用现场气力输送高压空气,提供该风量),在风速在3-18m/s条件下,沿提升管顶部由出口侧向出口相反侧水平送入。利用该气流将提升管顶部依靠约束结构分离的颗粒携带,经下行管道(用于回流颗粒下行的管道或隔板2)送入提升管底部,进而增强提升管颗粒的内部循环效果。The present invention guides the gas from the fan outlet of the riser system to the top of the riser (a small fan can also be added or directly use the on-site pneumatic power to transport high-pressure air to provide the air volume). The top of the tube is fed horizontally from the outlet side to the opposite side of the outlet. The air flow is used to carry the particles separated by the restraint structure at the top of the riser, and send them to the bottom of the riser through the downpipe (the pipe or
顶部循环气体流量与塔体直径直接有关:计算方法如下式:The top circulation gas flow rate is directly related to the diameter of the tower body: the calculation method is as follows:
式中:In the formula:
Qz为总处理烟气量,Nm3/h;Qz is the total flue gas volume, Nm3/h;
r-为当量直径,m;r- is the equivalent diameter, m;
α-修正系数,一般取1-2,当颗粒物料含湿量小于10%时取1,当含湿量小于18%时取1.5;小于22%时取2;α-correction coefficient, generally take 1-2, take 1 when the moisture content of the granular material is less than 10%, take 1.5 when the moisture content is less than 18%; take 2 when the moisture content is less than 22%;
ε-为经验系数,一般取0.2-0.4;当回送气体压力小于2000Pa时选较大值;当回送气提压力高于2000Pa时可取较小值。ε- is an empirical coefficient, generally 0.2-0.4; when the return gas pressure is less than 2000Pa, choose a larger value; when the return gas lift pressure is higher than 2000Pa, you can take a smaller value.
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JP2001221405A (en) * | 2000-02-08 | 2001-08-17 | Mitsubishi Heavy Ind Ltd | Circulating type fluidized bed combustion furnace |
CN2487738Y (en) * | 2001-06-29 | 2002-04-24 | 辽宁省能源研究所 | Partition board type internal circulation fluidized bed gasification furnace |
CN2931477Y (en) * | 2006-07-31 | 2007-08-08 | 中国科学院广州能源研究所 | A clapboard type internal circulating fluidized bed gasifier with side air inlet |
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2010
- 2010-12-21 CN CN 201010598455 patent/CN102078782B/en not_active Expired - Fee Related
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001221405A (en) * | 2000-02-08 | 2001-08-17 | Mitsubishi Heavy Ind Ltd | Circulating type fluidized bed combustion furnace |
CN2487738Y (en) * | 2001-06-29 | 2002-04-24 | 辽宁省能源研究所 | Partition board type internal circulation fluidized bed gasification furnace |
CN2931477Y (en) * | 2006-07-31 | 2007-08-08 | 中国科学院广州能源研究所 | A clapboard type internal circulating fluidized bed gasifier with side air inlet |
Non-Patent Citations (1)
Title |
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党小庆等: "《大气污染控制工程技术与实践》", 30 April 2009 * |
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