[go: up one dir, main page]

CN209084801U - A flue gas moisture collection device - Google Patents

A flue gas moisture collection device Download PDF

Info

Publication number
CN209084801U
CN209084801U CN201821492048.9U CN201821492048U CN209084801U CN 209084801 U CN209084801 U CN 209084801U CN 201821492048 U CN201821492048 U CN 201821492048U CN 209084801 U CN209084801 U CN 209084801U
Authority
CN
China
Prior art keywords
flue gas
heat
collection device
chimney
moisture collection
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201821492048.9U
Other languages
Chinese (zh)
Inventor
钱江波
张子玉
孔祥灿
谷青峰
姚灏
于越
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
North China Electric Power University
Original Assignee
North China Electric Power University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by North China Electric Power University filed Critical North China Electric Power University
Priority to CN201821492048.9U priority Critical patent/CN209084801U/en
Application granted granted Critical
Publication of CN209084801U publication Critical patent/CN209084801U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/30Technologies for a more efficient combustion or heat usage

Landscapes

  • Chimneys And Flues (AREA)

Abstract

The utility model discloses a kind of flue gas moisture collection device, including heat pipe, the heat of flue gas is spilt into environment for exchanging heat to flue gas by heat pipe.As shown in the above, the design of the device is relatively simple, i.e., absorbs the heat in flue gas by heat pipe, and then the vapor in flue gas is made to liquefy so as to subsequent recovery;Meanwhile the heat in flue gas being discharged into environment by heat pipe.The flue gas moisture removal process can control the increase of smoke evacuation resistance as far as possible, and device design is simple.Therefore, the utility model proposes flue gas moisture collection device, can control discharge fume resistance under the premise of, simplify flue gas moisture removal process, improve recovery efficiency, solve the problems, such as the field at this stage.

Description

一种烟气水分收集装置A flue gas moisture collection device

技术领域technical field

本实用新型涉及烟气处理技术领域,更具体地说,涉及一种烟气水分收集装置。The utility model relates to the technical field of flue gas treatment, in particular to a flue gas moisture collection device.

背景技术Background technique

目前,世界上大多数电厂直接将脱硫脱硝后的烟气排入大气,进而使烟气中所含的大量水蒸气随之排入环境;而这些水蒸气中含有少量氮氧化物和硫氧化物,随意排放不仅造成了极大的水资源浪费,同时加剧了雾霾。At present, most power plants in the world directly discharge the flue gas after desulfurization and denitrification into the atmosphere, and then discharge a large amount of water vapor contained in the flue gas into the environment; and these water vapors contain a small amount of nitrogen oxides and sulfur oxides. , the random discharge not only causes a great waste of water resources, but also aggravates the haze.

就现有技术而言,烟气水蒸气收集装置大致可分为两类:一类设计为换热器,即利用冷却水等对烟气进行冷却,使水蒸气凝结,并予以回收,但是该技术较为复杂,运行成本较高;另一类是尚处于研究阶段的膜分离技术,即利用半透膜对烟气中水分进行分离、富集和提纯,该技术虽然能降低成本、提高收集率,但是会使排烟阻力大幅度增加,导致排烟状态恶化、增加其他设备的损耗。As far as the prior art is concerned, the flue gas water vapor collection devices can be roughly divided into two categories: one is designed as a heat exchanger, that is, the flue gas is cooled by cooling water, etc., so that the water vapor is condensed and recovered. The technology is more complex and the operating cost is high; the other is the membrane separation technology that is still in the research stage, that is, the use of semi-permeable membranes to separate, enrich and purify the moisture in the flue gas. Although this technology can reduce costs and improve collection rates , but it will greatly increase the smoke exhaust resistance, resulting in the deterioration of the exhaust state and the increase in the loss of other equipment.

因此,如何在控制排烟阻力的前提下,简化烟气水分回收过程,提高回收效率,是现阶段该领域亟待解决的难题。Therefore, how to simplify the flue gas moisture recovery process and improve the recovery efficiency under the premise of controlling the smoke exhaust resistance is an urgent problem to be solved in this field at this stage.

实用新型内容Utility model content

有鉴于此,本实用新型的目的在于提供一种烟气水分收集装置,该装置能够在控制排烟阻力的前提下,简化烟气水分回收过程,解决了现阶段该领域的难题。In view of this, the purpose of the present invention is to provide a flue gas moisture collection device, which can simplify the flue gas moisture recovery process under the premise of controlling the smoke exhaust resistance, and solve the current problems in this field.

一种烟气水分收集装置,包括热管,所述热管用于对烟气进行换热,并将烟气的热量散入环境。A flue gas moisture collection device includes a heat pipe, which is used for exchanging heat for the flue gas and dissipating the heat of the flue gas into the environment.

优选的,所述的烟气水分收集装置,所述热管包括:Preferably, in the flue gas moisture collection device, the heat pipe includes:

蒸发段,所述蒸发段位于烟囱内,用于吸收烟气的热量;an evaporation section, which is located in the chimney and is used to absorb the heat of the flue gas;

冷凝段,所述冷凝段位于烟囱外,用于将烟气的热量散入环境;The condensation section, which is located outside the chimney, is used to dissipate the heat of the flue gas into the environment;

绝热段,所述绝热段穿过所述烟囱的壁面,用于连接所述蒸发段和所述冷凝段。an adiabatic section, which passes through the wall of the chimney and is used to connect the evaporation section and the condensation section.

优选的,所述的烟气水分收集装置,还包括用于收集烟气中水分的收集器,所述收集器为环状,所述收集器的外边缘与所述烟囱的内壁相贴合,且所述收集器上设有集水孔。Preferably, the flue gas moisture collection device further includes a collector for collecting moisture in the flue gas, the collector is annular, and the outer edge of the collector is in contact with the inner wall of the chimney, And the collector is provided with a water collecting hole.

优选的,所述的烟气水分收集装置,还包括与所述集水孔相连通的下降管,所述下降管用于收集烟气中的水分凝结成的液体。Preferably, the flue gas moisture collection device further comprises a down pipe connected with the water collecting hole, and the down pipe is used for collecting the liquid condensed from the moisture in the flue gas.

优选的,所述的烟气水分收集装置,所述收集器呈倾斜状设置于所述烟囱内,所述集水孔位于所述收集器地势最低的位置。Preferably, in the flue gas moisture collecting device, the collector is disposed in the chimney in an inclined shape, and the water collecting hole is located at the lowest position of the collector.

优选的,所述的烟气水分收集装置,所述蒸发段的内壁上设有肋片。Preferably, in the flue gas moisture collection device, ribs are provided on the inner wall of the evaporation section.

优选的,所述的烟气水分收集装置,所述肋片沿烟囱的方向设置于所述蒸发段的内壁。Preferably, in the flue gas moisture collection device, the fins are arranged on the inner wall of the evaporation section along the direction of the chimney.

优选的,所述的烟气水分收集装置,所述肋片为多个,且多个所述肋片呈环状排列于所述蒸发段的内壁。Preferably, in the flue gas moisture collection device, there are multiple fins, and the multiple fins are arranged in a ring shape on the inner wall of the evaporation section.

优选的,所述的烟气水分收集装置,所述肋片呈倒三角状。Preferably, in the flue gas moisture collecting device, the fins are in the shape of an inverted triangle.

优选的,所述的烟气水分收集装置,所述烟气水分收集装置设置在所述烟囱的中部、或者上部。Preferably, in the flue gas moisture collecting device, the flue gas moisture collecting device is arranged in the middle or the upper part of the chimney.

本实用新型提出的烟气水分收集装置,包括热管,热管用于对烟气进行换热,并将烟气的热量散入环境。由上述内容可知,该装置的设计较为简单,即通过热管吸收烟气内的热量,进而使烟气内的水蒸气液化以便后续回收;同时,将烟气内的热量通过热管排入环境中。该烟气水分回收过程,能够尽量控制排烟阻力的增加,且装置设计简单。因此,本实用新型提出的烟气水分收集装置,能够在控制排烟阻力的前提下,简化烟气水分回收过程,提高回收效率,解决了现阶段该领域的难题。The flue gas moisture collection device proposed by the utility model includes a heat pipe, which is used for exchanging heat for the flue gas and dissipating the heat of the flue gas into the environment. It can be seen from the above that the design of the device is relatively simple, that is, the heat in the flue gas is absorbed by the heat pipe, and the water vapor in the flue gas is liquefied for subsequent recovery; at the same time, the heat in the flue gas is discharged into the environment through the heat pipe. The flue gas moisture recovery process can control the increase of the smoke exhaust resistance as much as possible, and the device design is simple. Therefore, the flue gas moisture collection device proposed by the present utility model can simplify the flue gas moisture recovery process and improve the recovery efficiency under the premise of controlling the smoke exhaust resistance, and solve the difficult problems in this field at the present stage.

附图说明Description of drawings

为了更清楚地说明本实用新型实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本实用新型的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the embodiments of the present utility model or the technical solutions in the prior art, the following briefly introduces the accompanying drawings that need to be used in the description of the embodiments or the prior art. Obviously, the accompanying drawings in the following description These are just some embodiments of the present invention, and for those of ordinary skill in the art, other drawings can also be obtained from these drawings without creative effort.

图1为本实用新型具体实施方式中热管示意图;1 is a schematic diagram of a heat pipe in a specific embodiment of the present invention;

图2为本实用新型具体实施方式中热管的简易图;2 is a simplified diagram of a heat pipe in a specific embodiment of the present invention;

图3为本实用新型具体实施方式中肋片示意图;3 is a schematic diagram of a rib in a specific embodiment of the present utility model;

图4为本实用新型具体实施方式中收集器的示意图。4 is a schematic diagram of a collector in a specific embodiment of the present invention.

图1-图4中:In Figures 1-4:

蒸发段—1、冷凝段—2、绝热段—3、收集器—4、下降管—5、肋片—6、蒸汽联管—7、上升管束—8、液体联管—9、气相部分—10、液相部分—11、上联管—12、冷凝管—13、下联管—14。Evaporation section - 1, condensation section - 2, adiabatic section - 3, collector - 4, descending pipe - 5, fins - 6, steam joint pipe - 7, riser tube bundle - 8, liquid joint pipe - 9, gas phase part - 10. Liquid phase part-11, upper connecting pipe-12, condensing pipe-13, lower connecting pipe-14.

具体实施方式Detailed ways

本具体实施方式的核心在于提供一种烟气水分收集装置,该装置能够在控制排烟阻力的前提下,简化烟气水分回收过程,解决了现阶段该领域的难题。The core of this specific embodiment is to provide a flue gas moisture collection device, which can simplify the flue gas moisture recovery process on the premise of controlling the smoke exhaust resistance, and solve the current difficulties in this field.

以下,参照附图对实施例进行说明。此外,下面所示的实施例不对权利要求所记载的实用新型内容起任何限定作用。另外,下面实施例所表示的构成的全部内容不限于作为权利要求所记载的实用新型的解决方案所必需的。Hereinafter, the embodiment will be described with reference to the drawings. In addition, the embodiments shown below do not have any limiting effect on the content of the utility model described in the claims. In addition, the whole content of the structure shown in the following embodiment is not limited to what is necessary for the solution of the invention described in the claim.

本具体实施方式提供的烟气水分收集装置,请参见图1-3;包括热管,该热管用于对烟气进行换热,并将烟气的热量散入环境。由上述内容可知,该装置的设计较为简单,即通过热管吸收烟气内的热量,进而使烟气内的水蒸气液化以便后续回收;同时,将烟气内的热量通过热管排入环境中。该烟气水分回收过程,不会增加烟气的阻力,且装置设计简单;较业内现有的设计,该设计能够尽可能减小会增加的烟阻。因此,本实用新型提出的烟气水分收集装置,能够在控制排烟阻力的前提下,简化烟气水分回收过程,解决了现阶段该领域的难题。The flue gas moisture collection device provided by this specific embodiment is shown in FIGS. 1-3 ; it includes a heat pipe, and the heat pipe is used for exchanging the heat of the flue gas and dissipating the heat of the flue gas into the environment. It can be seen from the above that the design of the device is relatively simple, that is, the heat in the flue gas is absorbed by the heat pipe, and the water vapor in the flue gas is liquefied for subsequent recovery; at the same time, the heat in the flue gas is discharged into the environment through the heat pipe. The flue gas moisture recovery process does not increase the resistance of the flue gas, and the device design is simple; compared with the existing designs in the industry, the design can reduce the increased smoke resistance as much as possible. Therefore, the flue gas moisture collecting device proposed by the present utility model can simplify the flue gas moisture recovery process under the premise of controlling the smoke exhaust resistance, and solve the problems in this field at the present stage.

需要说明的是,热管又称热导管,是一种具有快速均温特性的特殊材料,其为中空的金属管体,具有质轻的特点,且具备快速均温的特性,使其具有优异的热超导性能。典型的热管由管壳、吸液芯和端盖组成,将热管内抽成1.3×(10-1-10-4)Pa的负压后充以适量的工作液体,使紧贴管内壁的吸液芯毛细多孔材料中充满液体后加以密封。热管的一端为蒸发段1,另一端为冷凝段2,根据应用需要在两段中间可以设置绝热段3。当高温烟气流过时,热管一端的蒸发段1吸热使吸液芯中的液体蒸发汽化,蒸汽在微小的压差下,穿过绝热段3流向另一端的冷凝段2,并放出热量凝结成液体,液体再沿多孔材料依靠毛细作用及重力的作用流回蒸发段1。如此循环,将热量由热管的一端传至另一端,即将高温烟气的热量由烟囱内带至烟囱外,并将热量散热环境。It should be noted that a heat pipe, also known as a heat pipe, is a special material with rapid temperature uniformity. It is a hollow metal pipe body, which is light in weight and has rapid temperature uniformity, making it excellent Thermal superconductivity. A typical heat pipe consists of a tube shell, a liquid wick and an end cap. The heat pipe is pumped to a negative pressure of 1.3×(10 -1 -10 -4 )Pa and then filled with an appropriate amount of working liquid to make the suction close to the inner wall of the tube. The wick capillary porous material is filled with liquid and then sealed. One end of the heat pipe is the evaporation section 1, and the other end is the condensation section 2, and an adiabatic section 3 can be set between the two sections according to application requirements. When the high-temperature flue gas flows through, the evaporation section 1 at one end of the heat pipe absorbs heat to make the liquid in the liquid wick evaporate and vaporize. The liquid flows back to the evaporation section 1 along the porous material by capillary action and gravity. In this way, the heat is transferred from one end of the heat pipe to the other end, that is, the heat of the high-temperature flue gas is carried from the inside of the chimney to the outside of the chimney, and the heat is dissipated to the environment.

本具体实施方式提供的烟气水分收集装置,热管可以包括:蒸发段1,冷凝段2,绝热段3;其中,蒸发段1位于烟囱内,可以为紧贴烟囱内壁的布置形式,用于吸收烟气的热量;冷凝段2位于烟囱外,用于将烟气的热量散入环境;绝热段3用于连接蒸发段1和冷凝段2,且绝缘段需要穿过烟囱壁面,并可以采用水平的布置形式。另绝热段穿过墙体的部分可以采用水平或者倾斜的布置形式,或者其他能够起到同等效果的布置形式,只是在一般电场中采用水平布置更加便于施工,更贴近实际现场。In the flue gas moisture collection device provided by this specific embodiment, the heat pipe may include: an evaporation section 1, a condensation section 2, and an adiabatic section 3; wherein, the evaporation section 1 is located in the chimney, and can be arranged close to the inner wall of the chimney for absorbing The heat of the flue gas; the condensation section 2 is located outside the chimney and is used to dissipate the heat of the flue gas into the environment; the adiabatic section 3 is used to connect the evaporation section 1 and the condensation section 2, and the insulation section needs to pass through the wall of the chimney, and can be used horizontally. layout form. In addition, the part of the insulation section passing through the wall can be arranged in a horizontal or inclined arrangement, or other arrangements that can achieve the same effect, but in a general electric field, horizontal arrangement is more convenient for construction and closer to the actual site.

如此布置有以下优点:首先,热管式的换热结构简单,系统安全性能够得到保障,即使布置在较高的位置也不易引起严重的安全问题;其次,热管的蒸发段1从烟气中吸热,并通过冷凝段2向大气环境放热,布置在较高的位置可消除散热对地面人员及设备的影响;最后,热管散热表面与空气处于对流状态,烟囱是电厂中距离地面最高的设备,空气离地面越高,气温越低、风速越大,热管表面的对流换热系数就越大,冷凝段2的散热情况较为优越,使热管的冷产量增加、对烟气的冷却效果也就越好,因此,以将热管布置在烟囱较高的位置为益,如烟囱的中部或者上部。This arrangement has the following advantages: first, the heat exchange structure of the heat pipe type is simple, the safety of the system can be guaranteed, and even if it is arranged in a high position, it is not easy to cause serious safety problems; secondly, the evaporation section 1 of the heat pipe sucks from the flue gas The heat is released to the atmosphere through the condensation section 2, and it is arranged in a high position to eliminate the influence of heat dissipation on ground personnel and equipment; finally, the heat dissipation surface of the heat pipe is in a state of convection with the air, and the chimney is the equipment with the highest distance from the ground in the power plant. , the higher the air is from the ground, the lower the temperature and the greater the wind speed, the greater the convective heat transfer coefficient on the surface of the heat pipe, and the heat dissipation of the condensing section 2 is better, which increases the cooling output of the heat pipe and reduces the cooling effect on the flue gas. The better, therefore, it is beneficial to arrange the heat pipe in a higher position of the chimney, such as the middle or upper part of the chimney.

本具体实施方式提供的烟气水分收集装置,还可以包括用于收集烟气中水分的收集器4,用于收集蒸发段1冷凝的高温水蒸气。收集器4为环状、或称其为水槽,收集器4的外边缘与烟囱的内壁相贴合,且收集器4上设有集水孔。在烟囱内部,当烟气通过热管的蒸发段1时,会与高温烟气发生换热,吸收烟气中的热量,使烟气中的水蒸气液化并凝结,并附着于壁面。首先,形成由若干水分子聚集的核,随着蒸汽的不断冷凝和水蒸气在核表面的附着让成核的水蒸气分子团不断生长,长大后形成的水滴具有一定重量,在重力作用下沿着壁面流到收集器4内,在这个过程中大水滴可以带走壁面上附着的一部分小水滴。该设置能够及时收集并汇聚高温水蒸气凝结成的水滴。The flue gas moisture collection device provided in this specific embodiment may further include a collector 4 for collecting moisture in the flue gas, for collecting high-temperature water vapor condensed in the evaporation section 1 . The collector 4 is annular, or called a water tank, the outer edge of the collector 4 is in contact with the inner wall of the chimney, and the collector 4 is provided with a water collecting hole. Inside the chimney, when the flue gas passes through the evaporation section 1 of the heat pipe, it will exchange heat with the high-temperature flue gas, absorb the heat in the flue gas, liquefy and condense the water vapor in the flue gas, and adhere to the wall. First, a nucleus is formed that is composed of several water molecules. With the continuous condensation of steam and the adhesion of water vapor on the surface of the nucleus, the nucleated water vapor molecular clusters continue to grow, and the water droplets formed after growth have a certain weight. Under the action of gravity It flows into the collector 4 along the wall surface, and in this process, the large water droplets can take away a part of the small water droplets attached to the wall surface. This setting can collect and gather water droplets condensed from high temperature water vapor in time.

本具体实施方式提供的烟气水分收集装置,还可以包括与集水孔相连通的下降管5,下降管5用于将收集的液体由烟囱高处输送至底部,以待处理,以便于尽可能多的将烟气中的水分收集起来,以备后续处理。收集器4可以呈倾斜状设置于烟囱内,集水孔位于收集器4地势最低的位置,以便对凝结液进行收集。需要说明的是,上述需要收集的是烟气中水分凝结汇聚成的液体,即凝结液;此凝结液为混合物,即烟气中一些净化后仍残留的灰颗粒以及二氧化硫和氮氧化物会附着或溶解在水中,形成含有杂质的凝结水。The flue gas moisture collection device provided by this specific embodiment may also include a downcomer 5 communicated with the water collecting hole, and the downcomer 5 is used to transport the collected liquid from the height of the chimney to the bottom for treatment, so as to facilitate the exhaustion of the collected liquid. It is possible to collect more moisture in the flue gas for subsequent treatment. The collector 4 can be disposed in the chimney in an inclined shape, and the water collecting hole is located at the lowest position of the collector 4 so as to collect the condensate. It should be noted that what needs to be collected above is the liquid condensed and gathered by the moisture in the flue gas, that is, the condensate; this condensate is a mixture, that is, some remaining ash particles in the flue gas after purification, as well as sulfur dioxide and nitrogen oxides will adhere. Or dissolve in water to form condensate containing impurities.

本具体实施方式提供的烟气水分收集装置,蒸发段1的内壁上可以设有肋片6。紧贴壁面布置的蒸发管束其换热面积有限,即使采用多层布置的结构,但是一部分水蒸气仍会随烟气直接从主流区(即烟囱横截面中心处)掠过,来不及与热管进行换热就流出烟囱。因为烟囱中心处的水蒸汽浓度较高,故在中心增加换热表面不仅能够大幅度增加蒸汽换热的有效面积,还能提高热管管内工质的吸热量(即增加烟气的散热量)、降低烟气温度、提高水蒸气的凝结率。因此,在原设计的基础上可以设置肋片6以增强烟气中水蒸气的凝结效果。进一步,肋片6可以设置在每根蒸发管上,蒸发管即蒸发段1内工质流经的管道,径向布置呈倒三角的形式,也可以在其表面添加纹路,让水滴沿着换热表面向下流动,最终汇聚于水槽中。另肋片的设计不是必须的,其形状亦可以为能够起到相同效果的其他设计。本具体实施方式中的肋片只是以倒三角状为例,这种形状的肋片有利于换热和水分的收集。肋片6的布置形式应该依照实际情况进行布置,可以是其他的形式,其实际效果以能够增加换热表面、增加蒸汽凝结几率、减小烟气阻力为原则。肋片6沿烟囱的方向设置于蒸发段1的壁面上,如图3所示。In the flue gas moisture collection device provided by this specific embodiment, fins 6 may be provided on the inner wall of the evaporation section 1 . The heat exchange area of the evaporating tube bundle arranged close to the wall is limited. Even if the multi-layer structure is used, a part of the water vapor will still pass directly from the mainstream area (ie the center of the cross section of the chimney) with the flue gas, and it is too late to exchange with the heat pipe. The heat flows out of the chimney. Because the water vapor concentration at the center of the chimney is high, increasing the heat exchange surface in the center can not only greatly increase the effective area of steam heat exchange, but also increase the heat absorption of the working fluid in the heat pipe (that is, increase the heat dissipation of the flue gas). , Reduce the flue gas temperature and increase the condensation rate of water vapor. Therefore, on the basis of the original design, fins 6 can be provided to enhance the condensation effect of water vapor in the flue gas. Further, the fins 6 can be arranged on each evaporating tube. The evaporating tube is the pipeline through which the working medium flows in the evaporating section 1. The radial arrangement is in the form of an inverted triangle, and textures can also be added on the surface to allow the water droplets to follow the changing direction. The hot surface flows down and eventually converges in the sink. In addition, the design of the rib is not necessary, and its shape can also be other designs that can achieve the same effect. The fins in this specific embodiment are only in an inverted triangle shape as an example, and the fins in this shape are beneficial to heat exchange and moisture collection. The arrangement form of the fins 6 should be arranged according to the actual situation, and can be in other forms. The fins 6 are arranged on the wall surface of the evaporation section 1 along the direction of the chimney, as shown in FIG. 3 .

本具体实施方式提供的烟气水分收集装置,肋片6为多个,且多个肋片6呈环状排列于蒸发段1的内壁。例如,肋片6可以为薄片且呈倒三角状,在换热和增大蒸气凝结面积的同时能够有效降低烟气的流动阻力,如图2所示。In the flue gas moisture collecting device provided by this specific embodiment, there are multiple fins 6 , and the multiple fins 6 are arranged on the inner wall of the evaporation section 1 in a ring shape. For example, the fins 6 can be thin sheets and have an inverted triangular shape, which can effectively reduce the flow resistance of the flue gas while exchanging heat and increasing the vapor condensation area, as shown in FIG. 2 .

进一步,分别对热管的蒸发段1、绝热段3及冷凝段2进行详细介绍:蒸发段1Further, the evaporation section 1, the adiabatic section 3 and the condensation section 2 of the heat pipe are introduced in detail: evaporation section 1

如图2是热管蒸发段1的布置结构,包括上端的蒸汽联管7、周向布置的上升管束8以及下端的液体联管9三部分;其中,蒸发段1管束布置位置相对较低,整个蒸发段1换热面的工质在重力的作用下都保持在液相状态,从而形成持续良好的换热效果。在烟气侧,蒸发段1内部,周向贴壁布置的上升管束8内工质会使靠近壁面附近的水蒸气首先凝结,然后在分压力梯度(即浓度差)的作用下,烟气中的水蒸气会形成从中心向壁面扩散的趋势。虽然烟气主流区中心处的水蒸气周向扩散,但中心处的水蒸气浓度仍最高,通过增加换热面的级数能够实现对烟气水蒸气的逐级回收过程,尽可能多的使水蒸气凝结。Figure 2 shows the arrangement structure of the evaporation section 1 of the heat pipe, which includes three parts: the steam header 7 at the upper end, the rising tube bundle 8 arranged in the circumferential direction, and the liquid header 9 at the lower end. Under the action of gravity, the working medium on the heat exchange surface of the evaporation section 1 is kept in the liquid phase, thus forming a continuous and good heat exchange effect. On the flue gas side, inside the evaporation section 1, the working fluid in the ascending tube bundle 8 arranged circumferentially close to the wall will cause the water vapor near the wall to condense first, and then under the action of the partial pressure gradient (ie the concentration difference), the flue gas will The water vapor will form a tendency to diffuse from the center to the wall. Although the water vapor in the center of the main flow area of flue gas diffuses circumferentially, the water vapor concentration in the center is still the highest. Water vapor condenses.

绝热段3Insulation section 3

如图2所示,热管的绝热段3是不参与换热的热管管段,其作用是完成蒸发段1和冷凝段2的联通和热管内部工质的输送,绝热段3的管束可分为两个部分:气相部分10和液相部分11。气相部分10连接蒸发段1的蒸汽联管7与冷凝段2的上联管12,使工质蒸汽由蒸发段1进入冷凝段2散热;液相部分11连接蒸发段1的液体联管9与冷凝段2的下联管14,使工质液体由冷凝段2进入蒸发段1吸热。As shown in Figure 2, the adiabatic section 3 of the heat pipe is a heat pipe section that does not participate in heat exchange. Its function is to complete the communication between the evaporation section 1 and the condensation section 2 and the transportation of the working fluid inside the heat pipe. The tube bundle of the adiabatic section 3 can be divided into two Parts: gas phase part 10 and liquid phase part 11. The gas phase part 10 connects the steam pipe 7 of the evaporation section 1 and the upper pipe 12 of the condensation section 2, so that the working medium steam enters the condensation section 2 from the evaporation section 1 for heat dissipation; the liquid phase part 11 is connected to the liquid pipe 9 of the evaporation section 1 and The downstream pipe 14 of the condensation section 2 makes the working fluid enter the evaporation section 1 from the condensation section 2 to absorb heat.

考虑到实际安装过程的可行性,绝热段3管道需要穿过烟囱以及烟囱的壁面,这些地方的管道可以采用水平布置形式,而高度差上采取垂直管道的形式、布置在烟囱管壁与烟囱混凝土支撑部分间的空隙,尽量减少在烟囱管壁和烟囱上开孔,以保证安全性、减小施工难度。Considering the feasibility of the actual installation process, the pipes in the insulation section 3 need to pass through the chimney and the wall of the chimney. The pipes in these places can be arranged horizontally, and the height difference can be in the form of vertical pipes, which are arranged between the chimney pipe wall and the chimney concrete. The gap between the supporting parts should be minimized by opening holes on the chimney pipe wall and chimney to ensure safety and reduce construction difficulty.

冷凝段2Condensing section 2

如图2所示,热管冷凝段2包括上联管12、冷凝管13和下联管14。工质蒸汽由上联管12分配,在压力差的推动下向下进入冷凝管13束进行降温凝结,再通过下联管14流进热管的绝热段3。因为热管布置的位置较高,因此,冷凝段2换热表面与空气属于高强度的对流换热,换热效果较为理想,冷凝段2的管束可采取弯管的样式使其稍远离烟囱表面,以减少边界层对其的影响,增强散热效果,使管内蒸汽工质迅速凝结成液态。As shown in FIG. 2 , the condensing section 2 of the heat pipe includes an upper connecting pipe 12 , a condensing pipe 13 and a lower connecting pipe 14 . The working fluid steam is distributed by the upper connecting pipe 12, and is pushed down by the pressure difference to enter the bundle of condenser pipes 13 for cooling and condensation, and then flows into the adiabatic section 3 of the heat pipe through the lower connecting pipe 14. Because the heat pipes are arranged at a relatively high position, the heat exchange surface of the condensation section 2 and the air belong to high-intensity convective heat exchange, and the heat exchange effect is ideal. In order to reduce the influence of the boundary layer on it, enhance the heat dissipation effect, and quickly condense the steam working medium in the tube into a liquid state.

对所公开的实施例的上述说明,使本领域专业技术人员能够实现或使用本实用新型。对这些实施例的多种修改对本领域的专业技术人员来说将是显而易见的,本文中所定义的一般原理可以在不脱离本实用新型的精神或范围的情况下,在其它实施例中实现。因此,本实用新型将不会被限制于本文所示的这些实施例,而是要符合与本文所公开的原理和新颖特点相一致的最宽的范围。The above description of the disclosed embodiments enables those skilled in the art to implement or use the present invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the generic principles defined herein may be implemented in other embodiments without departing from the spirit or scope of the present invention. Thus, the present invention is not intended to be limited to the embodiments shown herein, but is to be accorded the widest scope consistent with the principles and novel features disclosed herein.

Claims (9)

1. a kind of flue gas moisture collection device, which is characterized in that including heat pipe, the heat pipe is used to exchange heat to flue gas, and The heat of flue gas is spilt into environment;
The heat pipe includes:
Evaporator section (1), the evaporator section (1) is located in chimney, for absorbing the heat of flue gas;
Condensation segment (2), the condensation segment (2) is located at outside chimney, for the heat of flue gas to be spilt into environment;
Adiabatic section (3), the adiabatic section (3) passes through the wall surface of the chimney, for connecting the evaporator section (1) and the condensation Section (2).
2. flue gas moisture collection device according to claim 1, which is characterized in that further include for collecting moisture in flue gas Collector (4), the collector (4) is ring-type, and the inner wall of the outer edge and the chimney of the collector (4) fits, And the collector (4) is equipped with gully-hole.
3. flue gas moisture collection device according to claim 2, which is characterized in that further include being connected with the gully-hole Down-comer (5), the down-comer (5) be used to collect hydrogenesis in flue gas at liquid.
4. flue gas moisture collection device according to claim 2, which is characterized in that the collector (4) obliquely sets It is placed in the chimney, the gully-hole is located at the minimum position of the collector (4) topography.
5. flue gas moisture collection device according to claim 1, which is characterized in that set on the inner wall of the evaporator section (1) There are fin (6).
6. flue gas moisture collection device according to claim 5, which is characterized in that the fin (6) is along the direction of chimney It is set to the inner wall of the evaporator section (1).
7. flue gas moisture collection device according to claim 6, which is characterized in that the fin (6) is multiple and multiple The fin (6) is annularly arranged in the inner wall of the evaporator section (1).
8. flue gas moisture collection device according to claim 6, which is characterized in that the fin (6) is in inverted triangle shape.
9. flue gas moisture collection device according to claim 1, which is characterized in that the flue gas moisture collection device setting At the middle part or top of the chimney.
CN201821492048.9U 2018-09-12 2018-09-12 A flue gas moisture collection device Expired - Fee Related CN209084801U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201821492048.9U CN209084801U (en) 2018-09-12 2018-09-12 A flue gas moisture collection device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201821492048.9U CN209084801U (en) 2018-09-12 2018-09-12 A flue gas moisture collection device

Publications (1)

Publication Number Publication Date
CN209084801U true CN209084801U (en) 2019-07-09

Family

ID=67116427

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201821492048.9U Expired - Fee Related CN209084801U (en) 2018-09-12 2018-09-12 A flue gas moisture collection device

Country Status (1)

Country Link
CN (1) CN209084801U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108895479A (en) * 2018-09-12 2018-11-27 华北电力大学(保定) A kind of flue gas moisture collection device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108895479A (en) * 2018-09-12 2018-11-27 华北电力大学(保定) A kind of flue gas moisture collection device

Similar Documents

Publication Publication Date Title
CN107042048B (en) Gravity heat pipe type demisting method and demisting device
CN102313404A (en) Condenser with liquid separation type spiral tube structure
CN106968294A (en) A kind of bionic type energy-saving air captation
CN109519953B (en) A Flue Gas Waste Heat Utilization System of Power Plant Boiler with Flow Balance
CN204388641U (en) A kind of counter flow evaporative condenser
CN207003543U (en) A kind of bionic type energy-saving air captation
CN110124347A (en) A kind of energy and water saving type flue gas purification device and method
CN209084801U (en) A flue gas moisture collection device
CN110104716A (en) A kind of two-tube opposed type solar energy sea water desalination apparatus based on membrane distillation
CN105277005B (en) Corrugated plating condensing heat exchanger
CN106512691A (en) Desulfurized flue gas water recycling system
CN104864376A (en) Heat-pipe type falling film evaporation low-temperature waste heat utilization and water recovery equipment
CN110425510A (en) Parallel small-diameter heat pipe enhanced heat exchange device for recycling waste heat of medium-low temperature flue gas and preparation method thereof
CN108895479A (en) A kind of flue gas moisture collection device
CN107970637A (en) A kind of absorption tower and condensation receipts water dust removal method that water dust pelletizing system is received with condensation
CN210159324U (en) Cooling and dehumidifying combined smoke whitening device
CN107082462A (en) A kind of modified and reinforced tubular type fresh-water generator in surface
CN203724793U (en) Heat-pipe type solar heat-collecting and solution-regenerating integration device
RU96418U1 (en) SECTION AIR COOLING UNIT TYPE ABC GI WITH GAS COOLER
CN109870055A (en) A hot water storage tank utilizing waste heat of flue gas and using method thereof
CN105066763A (en) Heat exchange tube with special-shaped fins and turbulators and heat exchanger
CN103381302B (en) Heat pipe vacuum tube solar liquid regenerator
CN109519954B (en) A utility boiler flue gas waste heat utilization system
CN210331720U (en) Condensing device on top of distillation tower
CN208893962U (en) A kind of disturbing flow device for flue gas condensing

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20190709

Termination date: 20200912

CF01 Termination of patent right due to non-payment of annual fee