CN104482793A - Open rack vaporizer heat exchange tube capable of thermoelectrically recovering cold energy from LNG (Liquefied Natural Gas) - Google Patents

Open rack vaporizer heat exchange tube capable of thermoelectrically recovering cold energy from LNG (Liquefied Natural Gas) Download PDF

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CN104482793A
CN104482793A CN201410834464.2A CN201410834464A CN104482793A CN 104482793 A CN104482793 A CN 104482793A CN 201410834464 A CN201410834464 A CN 201410834464A CN 104482793 A CN104482793 A CN 104482793A
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heat exchange
lng
tube
open
thermoelectric material
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许佳伟
屈长龙
杨亮
明红芳
齐超
王博杰
王文
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China National Offshore Oil Corp CNOOC
CNOOC Gas and Power Group Co Ltd
Shanghai Jiao Tong University
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China National Offshore Oil Corp CNOOC
CNOOC Gas and Power Group Co Ltd
Shanghai Jiao Tong University
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Abstract

本发明涉及一种可热电回收LNG冷能的开架式气化器换热管,它包括有管体,所述管体的管壁内外均设置有强化换热结构翅片,靠近LNG的入口端的所述管体为所述开架式气化器的气化段,靠近LNG出口端的所述管体为所述开架式气化器的加热段;其特征在于:位于所述气化段的管体管壁上设置有一环状间隙,所述环状间隙内填充热电材料,对应所述环状间隙的位置,所述管体的管壁上还设置一用于防止所述热电材料泄露的端盖。本发明通过改变管内外换热流体传热温度差最大的换热管段的结构,有效调整其换热过程的局部热阻,控制冰层在换热器表面的生长,同时,热电材料回收LNG中的部分冷能并转化为电能。本发明可以广泛应用于换热管的制作过程中。

The invention relates to an open-frame gasifier heat exchange tube capable of recovering cold energy of LNG by thermoelectricity. The pipe body is the gasification section of the open-frame gasifier, and the pipe body near the LNG outlet end is the heating section of the open-frame gasifier; it is characterized in that: the pipe body located in the gasification section There is an annular gap on the tube wall, and the thermoelectric material is filled in the annular gap. Corresponding to the position of the annular gap, an end cap for preventing leakage of the thermoelectric material is also provided on the tube wall of the tube body . The invention effectively adjusts the local thermal resistance of the heat exchange process by changing the structure of the heat exchange tube section with the largest heat transfer temperature difference of the heat exchange fluid inside and outside the tube, controls the growth of the ice layer on the surface of the heat exchanger, and at the same time, recycles the thermoelectric material into the LNG Part of the cold energy is converted into electrical energy. The invention can be widely used in the production process of heat exchange tubes.

Description

一种可热电回收LNG冷能的开架式气化器换热管An open-frame gasifier heat exchange tube capable of thermoelectrically recovering LNG cold energy

技术领域technical field

本发明涉及一种开架式气化器换热管,特别是关于一种可热电回收LNG冷能的开架式气化器换热管。The invention relates to an open-frame gasifier heat exchange tube, in particular to an open-frame gasifier heat exchange tube capable of thermoelectrically recovering LNG cold energy.

背景技术Background technique

在LNG接收站或气化站中,常常需要将LNG加热至常温气体进入城市输运管道。开架式气化器(ORV)是一种以海水为热源的气化器,用于基本负荷型的大型气化装置,可以在0%~105%的负荷范围内安全运行,并能够根据需求的变化调整汽化量。ORV的基本单元是换热管,由若干换热管组成一个板状排列,两端由集气管或集液管焊接形成一个板型管束,再由若干个板型管束组成气化器,气化器顶部有海水喷淋装置,海水被喷淋在板型管束外表面上,依靠重力的作用自上而下流动。LNG在管内自下而上流动,在此过程中,海水将热量传递给LNG,使其加热并气化。In the LNG receiving station or gasification station, it is often necessary to heat the LNG to room temperature and the gas enters the urban transportation pipeline. The open rack vaporizer (ORV) is a gasifier that uses seawater as the heat source. It is used for large-scale base-load gasification devices. It can operate safely within the load range of 0% to 105%. Change to adjust the amount of vaporization. The basic unit of ORV is the heat exchange tube, which is composed of several heat exchange tubes in a plate-like arrangement, and the two ends are welded by gas collectors or liquid collectors to form a plate-shaped tube bundle, and then a gasifier is composed of several plate-shaped tube bundles. There is a seawater spraying device on the top of the device, and the seawater is sprayed on the outer surface of the plate-shaped tube bundle, and flows from top to bottom by gravity. LNG flows from bottom to top in the pipe, and in the process, seawater transfers heat to the LNG, heating it and gasifying it.

传统的ORV运行时在板型管束的下部都会结冰,尽管水膜沿管板下落的过程中具有较高的换热系数,但是由于冰层的导热系数远低于铝的导热系数,因此会使气化器的整体传热性能下降。为了改善管外结冰的问题及提高气化器的传热性能,SuperORV(超级开架式气化器)在传统的ORV基础上对换热管的结构进行了改进,在LNG气化段采用了双层结构的换热管结构。SuperORV的双层套管结构本质上是通过牺牲换热结构的紧凑性,增加传热热阻,减少局部换热温度差,达到冰层控制的目的。LNG在气化的过程中会释放大量的冷能,传统ORV和SuperORV在运行过程中,将这部分冷能直接释放,因此造成能量的浪费。为了改善管外结冰的问题及提高气化器的传热性能,有必要对ORV换热管的结构进行改进和优化。When the traditional ORV is running, the lower part of the plate-type tube bundle will freeze. Although the water film has a high heat transfer coefficient during the process of falling along the tube sheet, the thermal conductivity of the ice layer is much lower than that of aluminum, so it will Decrease the overall heat transfer performance of the gasifier. In order to improve the problem of icing outside the tube and improve the heat transfer performance of the gasifier, the SuperORV (Super Open Frame Gasifier) has improved the structure of the heat exchange tube on the basis of the traditional ORV. Double-layer heat exchange tube structure. The double-layer casing structure of SuperORV essentially sacrifices the compactness of the heat exchange structure, increases the heat transfer resistance, and reduces the local heat exchange temperature difference to achieve the purpose of ice layer control. During the gasification process of LNG, a large amount of cold energy will be released. During the operation of traditional ORV and SuperORV, this part of cold energy will be released directly, thus causing energy waste. In order to improve the problem of icing outside the tube and improve the heat transfer performance of the gasifier, it is necessary to improve and optimize the structure of the ORV heat exchange tube.

发明内容Contents of the invention

针对上述问题,本发明的目的是提供一种不仅能够改善管外结冰问题,而且能够回收LNG冷能的开架气化器换热管。In view of the above problems, the object of the present invention is to provide a heat exchange tube for an open-frame gasifier that can not only improve the freezing problem outside the tube, but also recover the cold energy of LNG.

为实现上述目的,本发明采取以下技术方案:一种可热电回收LNG冷能的开架式气化器换热管,其特征在于:它包括有管体,所述管体的管壁内外均设置有强化换热结构翅片,靠近LNG的入口端的所述管体为所述开架式气化器的气化段,靠近LNG出口端的所述管体为所述开架式气化器的加热段;位于所述气化段的管体管壁上设置有一环状间隙,所述环状间隙内填充热电材料;对应所述环状间隙的位置,所述管体的管壁上还设置一用于防止所述热电材料泄露的端盖。In order to achieve the above object, the present invention adopts the following technical solutions: an open-frame vaporizer heat exchange tube capable of thermoelectrically recovering LNG cold energy, which is characterized in that it includes a tube body, and the inside and outside of the tube wall of the tube body are arranged There are heat-enhancing structural fins, the tube near the LNG inlet is the gasification section of the open-frame gasifier, and the tube near the LNG outlet is the heating section of the open-frame gasifier; An annular gap is arranged on the tube wall of the gasification section, and the thermoelectric material is filled in the annular gap; corresponding to the position of the annular gap, an annular gap is arranged on the tube wall of the tube body for An end cap that prevents leakage of the thermoelectric material.

所述热电材料采用低导热系数的碲化铋热电材料,其长度和厚度根据实际需要进行设定。The thermoelectric material adopts bismuth telluride thermoelectric material with low thermal conductivity, and its length and thickness are set according to actual needs.

所述管体内还插设一用于强化换热的扰流元件。A turbulence element for enhancing heat exchange is also inserted in the tube body.

本发明由于采取以上技术方案,其具有以下优点:1、本发明由于在换热管气化段的管体管壁上设置有环状间隙,环状间隙内填充低导热系数的热电材料,通过改变管内外换热流体传热温度差最大的换热管段的结构,局部增加换热热阻,从而抑制冰层在开架式气化器表面的生长,同时,在换热管加热LNG的同时,热电材料回收LNG中的部分冷能并转化为电能。2、本发明由于将低导热系数的热电材料设置在海水侧和LNG侧的换热系数较高的管段,热电材料两侧的温度差较大,即温度梯度较大,热电材料在此区域的热电转换效率较高,因此可以提高能源的利用率。3、本发明由于在管体内插设扰流元件,因此可以加剧管内流体湍流强度,强化换热。4、本发明由于利用回收的冷能发电,驱动部分辅机,因此可以减少耗电,提高能源的利用率。本发明可以广泛应用于开架式气化器换热管的制作过程中。Because the present invention adopts the above technical scheme, it has the following advantages: 1. In the present invention, an annular gap is arranged on the tube wall of the gasification section of the heat exchange tube, and the thermoelectric material with low thermal conductivity is filled in the annular gap. Change the structure of the heat exchange tube section where the heat transfer temperature difference of the heat exchange fluid inside and outside the tube is the largest, and locally increase the heat transfer resistance, thereby inhibiting the growth of the ice layer on the surface of the open-frame gasifier. At the same time, while the heat exchange tube is heating the LNG, Thermoelectric materials recover part of the cold energy in LNG and convert it into electricity. 2. In the present invention, since the thermoelectric material with low thermal conductivity is arranged in the pipe section with higher heat transfer coefficient on the seawater side and the LNG side, the temperature difference on both sides of the thermoelectric material is relatively large, that is, the temperature gradient is relatively large, and the temperature of the thermoelectric material in this area is relatively large. The thermoelectric conversion efficiency is high, so the utilization rate of energy can be improved. 3. The present invention can intensify the turbulent flow intensity of the fluid in the tube and enhance the heat exchange because the turbulence element is inserted in the tube body. 4. Since the present invention utilizes recovered cold energy to generate electricity and drive some auxiliary machines, it can reduce power consumption and improve energy utilization. The invention can be widely used in the manufacturing process of the heat exchange tube of the open frame gasifier.

附图说明Description of drawings

图1是本发明结构示意图,其中,(a)是主视图,(b)是仰视图,(c)是沿图(b)中的A-A线的剖视示意图;Fig. 1 is a structural representation of the present invention, wherein, (a) is a front view, (b) is a bottom view, and (c) is a schematic sectional view along the A-A line in figure (b);

图2是本发明气化段的剖视示意图;Fig. 2 is a schematic cross-sectional view of the gasification section of the present invention;

图3是本发明剖视示意图,其中,(a)是气化段剖视示意图,(b)是加热段剖视示意图;Fig. 3 is a schematic sectional view of the present invention, wherein (a) is a schematic sectional view of a gasification section, and (b) is a schematic sectional view of a heating section;

图4是本发明实施例1热电材料的厚度分布示意图,其中,横坐标表示换热管的长度,单位是m;纵坐标表示热电材料厚度,单位是mm;4 is a schematic diagram of the thickness distribution of the thermoelectric material in Example 1 of the present invention, wherein the abscissa represents the length of the heat exchange tube in m; the ordinate represents the thickness of the thermoelectric material in mm;

图5是现有的SuperORV换热管沿换热管管长冰层厚度示意图,其中,横坐标表示换热管的长度,单位是m;纵坐标表示冰层厚度,单位是mm;Figure 5 is a schematic diagram of the thickness of the ice layer along the length of the existing SuperORV heat exchange tube, wherein the abscissa indicates the length of the heat exchange tube in m; the ordinate indicates the thickness of the ice layer in mm;

图6是本发明实施例2的热电转换效率随管长分布曲线示意图,其中,横坐标表示换热管的长度,单位是m;纵坐标表示热电转换效率,单位是%;6 is a schematic diagram of the distribution curve of thermoelectric conversion efficiency with tube length in Example 2 of the present invention, wherein the abscissa indicates the length of the heat exchange tube in m; the ordinate indicates the thermoelectric conversion efficiency in %;

图7是本发明实施例2的实验结果对比示意图,其中,“●”表示带热电材料的换热管,“▲”表示不带热电材料的换热管;横坐标表示换热管的长度,单位是m;纵坐标表示冰层厚度,单位是mm。Fig. 7 is a schematic diagram of the comparison of the experimental results of Example 2 of the present invention, wherein "●" indicates a heat exchange tube with a thermoelectric material, "▲" indicates a heat exchange tube without a thermoelectric material; the abscissa indicates the length of the heat exchange tube, The unit is m; the ordinate indicates the thickness of the ice layer, and the unit is mm.

具体实施方式Detailed ways

下面结合附图和实施例对本发明进行详细的描述。The present invention will be described in detail below in conjunction with the accompanying drawings and embodiments.

如图1~3所示,本发明的可热电回收LNG冷能的开架式气化器换热管与现有的开架式气化器换热管结构基本相同,均包括有管体,管壁内外均设置有强化换热结构翅片,靠近LNG的入口端的管体为开架式气化器的气化段,靠近LNG出口端的管体为开架式气化器的加热段;本发明的不同之处在于:气化段的管体管壁上设置有一环状间隙,环状间隙内填充热电材料1;对应环状间隙的位置,管体的管壁上还设置一用于防止热电材料1泄露的端盖2。As shown in Figures 1 to 3, the open-frame gasifier heat exchange tube capable of thermoelectrically recovering LNG cold energy of the present invention is basically the same structure as the existing open-frame gasifier heat exchange tube, both including a tube body and a tube wall Both inside and outside are equipped with enhanced heat exchange structure fins, the tube body near the LNG inlet end is the gasification section of the open-frame gasifier, and the tube body near the LNG outlet end is the heating section of the open-frame gasifier; the difference of the present invention The location is: there is an annular gap on the tube wall of the gasification section, and the thermoelectric material 1 is filled in the annular gap; corresponding to the position of the annular gap, a tube wall is also provided to prevent the thermoelectric material 1 from leaking. The end cap 2.

在一个优选的实施例中,热电材料1用于从LNG冷能中回收部分冷能,并将这部分冷能转化为电能,热电材料1可以采用低导热系数的碲化铋热电材料,其长度和厚度可以根据实际需要进行设定。In a preferred embodiment, the thermoelectric material 1 is used to recover part of the cold energy from the cold energy of LNG, and convert this part of cold energy into electrical energy. The thermoelectric material 1 can be a bismuth telluride thermoelectric material with low thermal conductivity, and its length And thickness can be set according to actual needs.

在一个优选的实施例中,环状间隙的高度和厚度可以根据实际需要进行设定。In a preferred embodiment, the height and thickness of the annular gap can be set according to actual needs.

在一个优选的实施例中,管体内还可以插设一用于强化换热的扰流元件。In a preferred embodiment, a flow turbulence element for enhancing heat exchange can also be inserted in the tube body.

下面通过具体实施例对本发明的可热电回收LNG冷能的开架式气化器换热管的使用过程进行详细介绍;The use process of the open frame gasifier heat exchange tube capable of recovering LNG cold energy by thermoelectricity of the present invention will be described in detail below through specific embodiments;

实施例1:Example 1:

1)设置换热管的长度为6m,管内当量直径为14mm,管内侧翅化比为3.0,管外侧翅化比为2.3,管外径为37mm,管厚度为8.5mm,管体内部插设有扰流元件,气化段长度为2.5m,加热段长度为3.5m,环状间隙高度为3.2m,环状间隙厚度分布从LNG入口端开始沿管体逐渐变薄,初始厚度为4.5mm;环状间隙内填充碲化铋热电材料,其厚度的分布随沿管体发生变化(如图4所示);1) The length of the heat exchange tube is set to 6m, the equivalent diameter inside the tube is 14mm, the finning ratio inside the tube is 3.0, the finning ratio outside the tube is 2.3, the outer diameter of the tube is 37mm, and the thickness of the tube is 8.5mm. There are spoiler elements, the length of the gasification section is 2.5m, the length of the heating section is 3.5m, the height of the annular gap is 3.2m, the thickness distribution of the annular gap gradually becomes thinner along the pipe body from the LNG inlet end, and the initial thickness is 4.5mm ; Bismuth telluride thermoelectric material is filled in the annular gap, and the distribution of its thickness changes along the tube body (as shown in Figure 4);

2)LNG入口端温度为113.15K,海水入口温度为284.95K;2) The temperature at the LNG inlet port is 113.15K, and the seawater inlet temperature is 284.95K;

3)LNG进入换热管的气化段,在气化段被海水加热气化,由于气化段填充有低导热系数的碲化铋热电材料,增加了换热热阻,因此能够控制冰层在开架式气化器气化段表面的生长,减少换热管冰层厚度,可以达到相同条件下SuperORV对于冰层的控制水平(如图5所示),同时,碲化铋热电材料可以回收部分冷能并将其转换为电能,该换热管在运行时,可以输出0.48kW电力,如果一个开架式气化器包括720根换热管,该开架式气化器在运行过程中,可以输出348.4kW电力;3) LNG enters the gasification section of the heat exchange tube, and is heated and gasified by seawater in the gasification section. Since the gasification section is filled with bismuth telluride thermoelectric materials with low thermal conductivity, the heat transfer resistance is increased, so the ice layer can be controlled. The growth on the surface of the gasification section of the open-frame gasifier can reduce the thickness of the ice layer of the heat exchange tube, and can achieve the control level of SuperORV on the ice layer under the same conditions (as shown in Figure 5). At the same time, the bismuth telluride thermoelectric material can be recycled Part of the cold energy is converted into electrical energy. The heat exchange tube can output 0.48kW of electricity during operation. If an open-frame gasifier includes 720 heat exchange tubes, the open-frame gasifier can output 0.48kW of electricity during operation. Output 348.4kW power;

4)经过气化段加热的LNG进入加热段进一步加热,转化为常温气体,进入输运管道进行传输,LNG出口端为温度281.5K。4) The LNG heated by the gasification section enters the heating section for further heating, transforms into normal temperature gas, and enters the transportation pipeline for transportation. The temperature at the LNG outlet is 281.5K.

实施例2:Example 2:

1)本实施例的结构与实施例1结构基本相同,不同的是:气化段长度为3m,环状间隙的高度为3.0m,环状间隙的厚度为3.2mm,环状间隙内填充厚度为3.2mm的碲化铋热电材料;1) The structure of this embodiment is basically the same as that of Embodiment 1, except that the length of the gasification section is 3m, the height of the annular gap is 3.0m, the thickness of the annular gap is 3.2mm, and the filling thickness in the annular gap is 3.2mm bismuth telluride thermoelectric material;

2)LNG进入换热管的气化段,在气化段被海水加热气化;2) LNG enters the gasification section of the heat exchange tube, and is heated and gasified by seawater in the gasification section;

3)经过气化段加热的LNG进入加热段进一步加热,转化为常温气体,换热管LNG出口达到277.2K,本发明一个换热管在运行的同时,还可以输出0.36kW电力,如果一个开架式气化器包括720根换热管,该开架式气化器在运行过程中,还可以输出261.2kW电力,其热电转换效率随着管长的增加、温差的减小而降低(如图6所示),平均转化效率为2.3%左右。3) The LNG heated by the gasification section enters the heating section for further heating and is transformed into normal temperature gas. The LNG outlet of the heat exchange tube reaches 277.2K. A heat exchange tube of the present invention can also output 0.36kW power while it is running. If an open frame The open-frame gasifier includes 720 heat exchange tubes. During operation, the open-frame gasifier can also output 261.2kW of electricity, and its thermoelectric conversion efficiency decreases with the increase of the tube length and the decrease of the temperature difference (as shown in Figure 6 Shown), the average conversion efficiency is about 2.3%.

如图7所示,将本实施例的换热管与现有的换热管进行对比试验得知,本发明(带热电材料1的换热管)的最大冰层厚度小于4mm,现有换热管(不带热电材料1的换热管)的最大冰层厚度达到7mm,由此可见,本发明能够有效调整其换热过程的局部热阻,控制冰层在开架式气化器表面的生长。As shown in Figure 7, the comparison test between the heat exchange tube of this embodiment and the existing heat exchange tube shows that the maximum ice layer thickness of the present invention (heat exchange tube with thermoelectric material 1) is less than 4mm, while the existing heat exchange tube The maximum thickness of the ice layer of the heat pipe (the heat exchange tube without the thermoelectric material 1) reaches 7 mm. It can be seen that the present invention can effectively adjust the local thermal resistance of the heat exchange process and control the ice layer on the surface of the open-frame gasifier. grow.

上述各实施例仅用于说明本发明,其中各部件的结构、连接方式和制作工艺等都是可以有所变化的,凡是在本发明技术方案的基础上进行的等同变换和改进,均不应排除在本发明的保护范围之外。The above-mentioned embodiments are only used to illustrate the present invention, wherein the structure, connection mode and manufacturing process of each component can be changed to some extent, and any equivalent transformation and improvement carried out on the basis of the technical solution of the present invention should not excluded from the protection scope of the present invention.

Claims (3)

1. one kind can be reclaimed the open-frame type gasifier heat exchanger tube of LNG cold energy by thermoelectricity, it is characterized in that: it includes body, enhanced heat exchange structure fin is provided with inside and outside the tube wall of described body, described body near the arrival end of LNG is the gasification section of described open-frame type gasifier, and the described body near the LNG port of export is the bringing-up section of described open-frame type gasifier; The body tube wall being positioned at described gasification section is provided with an annular gap, in described annular gap, fills thermoelectric material; The position of corresponding described annular gap, the tube wall of described body is also arranged an end cap for preventing described thermoelectric material from revealing.
2. a kind ofly as claimed in claim 1 can reclaim the open-frame type gasifier heat exchanger tube of LNG cold energy by thermoelectricity, it is characterized in that: described thermoelectric material adopts the bismuth telluride thermoelectric material of low thermal conductivity, and its length and thickness set according to actual needs.
3. a kind ofly as claimed in claim 1 or 2 can reclaim the open-frame type gasifier heat exchanger tube of LNG cold energy by thermoelectricity, it is characterized in that: also plug one in described body for the turbulent element of enhanced heat exchange.
CN201410834464.2A 2014-12-26 2014-12-26 Open rack vaporizer heat exchange tube capable of thermoelectrically recovering cold energy from LNG (Liquefied Natural Gas) Pending CN104482793A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
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CN105651104A (en) * 2016-01-04 2016-06-08 郑州轻工业学院 Anti-frosting LNG air-heated nanofluid heat exchange pipe
CN111157572A (en) * 2020-01-07 2020-05-15 西安石油大学 A method for predicting and measuring ice layer in heat transfer tube of submerged combustion gasifier

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US20130008637A1 (en) * 2011-07-08 2013-01-10 Aislamientos Suaval, S.A. Encasement for heat transfer fluid (htf) conduits
CN202793134U (en) * 2012-07-30 2013-03-13 四川空分设备(集团)有限责任公司 Efficient heat pipe for liquefied natural gas (LNG) vaporizer
CN204514152U (en) * 2014-12-26 2015-07-29 中国海洋石油总公司 A kind ofly can reclaim the open-frame type gasifier heat exchanger tube of LNG cold energy by thermoelectricity

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CN2602186Y (en) * 2002-09-24 2004-02-04 中国科学技术大学 Semiconductive temperature difference power generating and hydrogen production apparatus using cold energy of liquefied natural gas
US20130008637A1 (en) * 2011-07-08 2013-01-10 Aislamientos Suaval, S.A. Encasement for heat transfer fluid (htf) conduits
CN202793134U (en) * 2012-07-30 2013-03-13 四川空分设备(集团)有限责任公司 Efficient heat pipe for liquefied natural gas (LNG) vaporizer
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