CN1431451A - Condenser with shaped strengthened tubes supported by hollow ring and enhanced method for transferring heat - Google Patents
Condenser with shaped strengthened tubes supported by hollow ring and enhanced method for transferring heat Download PDFInfo
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- 238000000034 method Methods 0.000 title claims abstract description 11
- 239000012530 fluid Substances 0.000 claims abstract description 7
- 230000005494 condensation Effects 0.000 claims abstract description 6
- 238000009833 condensation Methods 0.000 claims abstract description 6
- 230000002708 enhancing effect Effects 0.000 claims abstract 3
- 230000000737 periodic effect Effects 0.000 claims description 5
- 230000008878 coupling Effects 0.000 claims 1
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- 238000005859 coupling reaction Methods 0.000 claims 1
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- 239000011800 void material Substances 0.000 abstract description 2
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- 238000003466 welding Methods 0.000 description 2
- QNRATNLHPGXHMA-XZHTYLCXSA-N (r)-(6-ethoxyquinolin-4-yl)-[(2s,4s,5r)-5-ethyl-1-azabicyclo[2.2.2]octan-2-yl]methanol;hydrochloride Chemical compound Cl.C([C@H]([C@H](C1)CC)C2)CN1[C@@H]2[C@H](O)C1=CC=NC2=CC=C(OCC)C=C21 QNRATNLHPGXHMA-XZHTYLCXSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
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- 239000000463 material Substances 0.000 description 1
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Abstract
本发明提供一种空心环支承异形强化管冷凝器,包括壳体、换热管、管间支承物,换热管安装在壳体内,管间支承物安装在换热管之间并与换热管相连接;所述管间支承物为空心环网板,以点支承或线支承连接方式支承换热管;所述换热管为非光滑壁面的异形传热管;可以是缩放管、菱形翅片管、横纹管或螺旋槽管;一种冷凝器传热强化方法,利用空心环网板的轴向流道空隙率高,流通横截面大,对壳程纵向流体的形体阻力极小,使蒸汽对冷流的传热温差损失降至最小,提高对冷流传热推动力;本发明可减少壳侧的蒸汽流动阻力,使蒸汽对冷流的传热温差损失降至最小,提高冷凝传热推动力,并可强化管内对流及管外冷凝的传热,提高总传热系数及冷凝器的传热性能。
The invention provides a hollow ring-supported special-shaped reinforced tube condenser, which includes a shell, a heat exchange tube, and a support between tubes. The heat exchange tube is installed in the shell, and the support between the tubes is installed between the heat exchange tubes and connected to the heat exchange The tubes are connected; the support between the tubes is a hollow ring mesh plate, and the heat exchange tube is supported by a point support or a line support connection; the heat exchange tube is a special-shaped heat transfer tube with a non-smooth wall surface; it can be a scaling tube, a rhombus Finned tube, cross-grained tube or spiral grooved tube; a method for enhancing heat transfer in a condenser, using a hollow ring plate with a high void ratio in the axial flow channel, a large flow cross section, and minimal physical resistance to the longitudinal fluid in the shell side , so that the heat transfer temperature difference loss of steam to cold flow is minimized, and the driving force of heat transfer to cold flow is improved; the invention can reduce the steam flow resistance on the shell side, minimize the heat transfer temperature difference loss of steam to cold flow, and improve condensation The driving force of heat transfer can strengthen the heat transfer of convection in the tube and condensation outside the tube, and improve the total heat transfer coefficient and the heat transfer performance of the condenser.
Description
技术领域technical field
本发明涉及换热器技术,特别涉及一种空心环支承异形强化管冷凝器及传热强化方法。The invention relates to heat exchanger technology, in particular to a hollow ring-supported special-shaped reinforced tube condenser and a heat transfer strengthening method.
背景技术Background technique
工业上使用的冷凝器有多种结构,在管间支承物结构方面,主要有单弓折流隔板、双弓折流隔板及碟环折流隔板等,目前常用的冷凝器以单弓折流隔板支承管束的结构较多,且换热管主要为光滑传热管,冷凝器管间蒸汽在折流板间往返折流冲刷管束,因折流造成的流体形体阻力大,蒸汽压降大,冷凝器壳侧出口的蒸汽压力远低于壳侧入口压力,致使壳侧出口段蒸汽温度较入口段有较大幅度的下降,减少了对管程流体的传热温差,降低了冷凝器的传热效率,同时光滑传热管的传热膜系数较低,这也是目前工业冷凝器传热性能低下的一个主要原因。专利号为89218385.3的中国实用新型“管壳式换热器管间支承物”公开了一种空心环网板,利用这种空心环网板作为管间支承物可使单相流体换热器的壳侧流体沿轴向流动,大幅减少往返折流造成的形体阻力损失,这种管间支承结构也可借鉴用于多相流的冷凝器,通过减少壳程蒸汽阻力,达到减少传热温差损失的目的。Condensers used in industry have a variety of structures. In terms of the structure of the support between the tubes, there are mainly single-bow baffles, double-bow baffles, and dish-ring baffles. The commonly used condensers are single There are many structures supporting tube bundles by bow baffles, and the heat exchange tubes are mainly smooth heat transfer tubes. The steam between the condenser tubes baffles back and forth between the baffles and scours the tube bundles. The fluid shape resistance caused by baffles is large, and the steam The pressure drop is large, and the steam pressure at the shell-side outlet of the condenser is much lower than the shell-side inlet pressure, resulting in a relatively large drop in the steam temperature at the shell-side outlet section compared with the inlet section, which reduces the heat transfer temperature difference to the tube-side fluid and reduces the The heat transfer efficiency of the condenser and the heat transfer film coefficient of the smooth heat transfer tube are low, which is also a main reason for the low heat transfer performance of the current industrial condenser. Patent No. 89218385.3 Chinese utility model "shell-and-tube heat exchanger tube support" discloses a hollow ring mesh plate, using this hollow ring mesh plate as a tube support can make the single-phase fluid heat exchanger The fluid on the shell side flows in the axial direction, which greatly reduces the loss of physical resistance caused by back-and-forth baffles. This support structure between tubes can also be used for reference in condensers for multi-phase flow. By reducing the steam resistance on the shell side, the loss of heat transfer temperature difference can be reduced. the goal of.
发明内容Contents of the invention
本发明的目的在于克服现有折流隔板式结构的冷凝器管间蒸汽流动阻力大,传热温差损失大,及光滑传热管传热膜系数小,传热性能差的缺点及不足,研究设计一种可有效降低壳程蒸汽流动阻力,减少传热温差损失,同时针对换热管内与管外传热热阻控制的具体情况,合理选择高效异形换热管,提高总传热系数的空心环支承异形强化管冷凝器。The purpose of the present invention is to overcome the disadvantages and deficiencies of the existing baffle-type structure of the condenser tubes of large steam flow resistance, large heat transfer temperature difference loss, small heat transfer film coefficient and poor heat transfer performance of smooth heat transfer tubes, Research and design a method that can effectively reduce the shell-side steam flow resistance and reduce the loss of heat transfer temperature difference. At the same time, according to the specific situation of heat transfer resistance control inside and outside the heat transfer tube, reasonably select high-efficiency special-shaped heat transfer tubes to improve the overall heat transfer coefficient. The hollow ring supports the special-shaped reinforced tube condenser.
本发明的另一目的在于提供一种应用于上述空心环支承异形强化管冷凝器的传热强化方法。Another object of the present invention is to provide a heat transfer enhancement method applied to the hollow ring-supported special-shaped enhanced tube condenser.
本发明的目的通过下述技术方案实现:本空心环支承异形强化管冷凝器包括壳体、换热管、管间支承物,换热管安装在壳体内,管间支承物安装在换热管之间并与换热管相连接;所述管间支承物为空心环网板,以点支承或线支承连接方式支承换热管。The purpose of the present invention is achieved through the following technical solutions: the hollow ring supported special-shaped reinforced tube condenser includes a shell, a heat exchange tube, and a support between the tubes, the heat exchange tube is installed in the shell, and the support between the tubes is installed on the heat exchange tube The space between them is connected with the heat exchange tubes; the support between the tubes is a hollow ring mesh plate, and the heat exchange tubes are supported by a point support or a line support connection.
所述管间支承物的结构形式为管节空心环或螺旋线空心环。The structural form of the support between pipes is a pipe joint hollow ring or a helical hollow ring.
所述换热管为非光滑壁面的异形传热管;可以是沿轴向带周期性扩张与收缩周向锥面形状变化的缩放管,或是沿轴向带周期性周向非连续三维翅片的菱形翅片管,或是沿轴向带周期性周向凹槽的横纹管或螺旋槽管。The heat exchange tube is a special-shaped heat transfer tube with a non-smooth wall surface; it can be a zoom tube with periodic expansion and contraction along the axial direction and a tapered shape change in the circumferential direction, or a periodical circumferential discontinuous three-dimensional fin along the axial direction. Diamond-shaped finned tubes, or horizontally or spirally grooved tubes with periodic circumferential grooves along the axial direction.
本发明的传热强化方法为:利用空心环网板的轴向流道空隙率高,流通横截面大,对壳程纵向流体的形体阻力极小,使蒸汽对冷流的传热温差损失降至最小,提高对冷流传热推动力。The heat transfer enhancement method of the present invention is as follows: the void ratio of the axial channel of the hollow ring screen plate is high, the flow cross section is large, and the physical resistance to the longitudinal fluid in the shell side is extremely small, so that the heat transfer temperature difference loss of the steam to the cold flow is reduced. To the minimum, improve the driving force of convective heat transfer.
所述传热强化方法可同时利用异形传热管的非光滑传热壁面强化管内及管外的对流传热与冷凝传热。The heat transfer enhancement method can simultaneously utilize the non-smooth heat transfer wall surface of the special-shaped heat transfer tube to enhance convective heat transfer and condensation heat transfer inside and outside the tube.
本发明与现有技术相比具有如下的优点和效果:①用空心环网板取代现有的折流隔板作为壳程管间支承物,可有效减少壳侧的蒸汽流动阻力,可使蒸汽对冷流的传热温差损失降至最小,提高冷凝传热推动力;②用异形传热管取代现有的光滑传热管,可强化管内对流及管外冷凝的传热,有效提高总传热系数,提高冷凝器的传热性能,在以上两项改进因素的作用下,冷凝器与现有技术相比,在传热工艺条件不变的情况下,可大幅减少冷凝器的面积与材耗,或在冷凝器面积不变的情况下大幅提高冷凝器的传热负荷。Compared with the prior art, the present invention has the following advantages and effects: ① Replace the existing baffle plate with the hollow ring screen as the support between the shell side tubes, which can effectively reduce the steam flow resistance on the shell side and make the steam The heat transfer temperature difference loss of the cold flow is minimized, and the driving force of condensation heat transfer is improved; ② The existing smooth heat transfer tube is replaced by a special-shaped heat transfer tube, which can strengthen the heat transfer of convection inside the tube and condensation outside the tube, and effectively improve the total heat transfer. The thermal coefficient improves the heat transfer performance of the condenser. Under the effect of the above two improvement factors, compared with the existing technology, the condenser can greatly reduce the area and material of the condenser when the heat transfer process conditions remain unchanged. consumption, or greatly increase the heat transfer load of the condenser when the condenser area remains the same.
附图说明Description of drawings
图1是空心环支承异形强化管冷凝器的结构示意图。Figure 1 is a schematic structural view of a hollow ring-supported special-shaped reinforced tube condenser.
图2是图1的A-A向剖视示意图。Fig. 2 is a schematic cross-sectional view along the line A-A of Fig. 1 .
图3是图1所用的空心环网板的结构示意图。Fig. 3 is a schematic structural view of the hollow ring screen used in Fig. 1 .
图4是图1所用的缩放管结构示意图。FIG. 4 is a schematic structural diagram of the zoom tube used in FIG. 1 .
图5是图1所用的菱形翅片管结构示意图。Fig. 5 is a schematic diagram of the structure of the rhombic finned tube used in Fig. 1 .
图6是图1所用的横纹槽管结构示意图。Fig. 6 is a schematic diagram of the structure of the horizontally grooved pipe used in Fig. 1 .
图7是图1所用的螺旋槽管结构示意图。Fig. 7 is a schematic diagram of the structure of the spirally grooved pipe used in Fig. 1 .
具体实施方式Detailed ways
下面结合附图及实施例对本发明作进一步详细的描述,但本发明的实施方式不限于此。The present invention will be described in further detail below with reference to the accompanying drawings and examples, but the embodiments of the present invention are not limited thereto.
实施例Example
图1及图2示出了本发明的具体结构,由图1所见,本空心环支承异形强化管冷凝器由换热器的壳侧蒸汽入口管1、壳侧入口环套2、空心环网板3、异形传热管4、冷凝器壳体5、下管板6、下封头7、冷流入口管8、壳侧凝液出口管9、上管板10、上封头11、冷流出口管12共同安装连接构成,其相互位置及连接关系为:异形传热管4与上、下管板10与6通过焊接或胀管相连接后置于冷凝器壳体5内,若干空心环网板3按一定的间距分布安置于传热管4之间,以点支承或线支承的方式支承异形传热管4,壳体蒸汽入口管1焊在壳侧入口环套2侧面,壳侧入口环套2与冷凝器壳体5焊接及与上管板10焊接,冷凝器壳体5下端与下管板6相焊,并在冷凝器壳体5侧面连接壳侧凝液出口管9,上、下管板10、6分别与上下封头11、7相连接,并与冷流入口8及出口12连接构成冷凝器的管程流道。其中:空心环网板4的形状如图3所示,结构形式为管节空心环,可以由短管节,纵横上下扁钢及边框焊接构成,也可以是由锻件冲压构成,或浇注模块构成;异形传热管4可以是如图4所示的沿轴向带周期性扩张与收缩周向锥面形状变化的缩放管;或是如图5所示的沿轴向带周期性周向非连续三维翅片的菱形翅片管;或是如图6所示的沿轴向带周期性周向凹槽的横纹管或如图7所示的螺旋槽管。Fig. 1 and Fig. 2 have shown the concrete structure of the present invention, seen by Fig. 1, this hollow ring support special-shaped strengthened tube condenser is made up of shell side steam inlet pipe 1 of heat exchanger, shell side
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100334416C (en) * | 2004-02-10 | 2007-08-29 | 华南理工大学 | Shell and tube type heat exchanger with sharply enlarged accelerated flow zooming tube bundle and hollow ring |
CN102322768A (en) * | 2011-09-06 | 2012-01-18 | 华南理工大学 | Sugar liquid pre-heating device adopting urgent expansion accelerated flow convergent-divergent pipe internally inserted with rotational flow sheets |
CN102425973A (en) * | 2011-10-29 | 2012-04-25 | 双良节能系统股份有限公司 | Lining strip heat exchanger |
CN103267435A (en) * | 2013-06-06 | 2013-08-28 | 国家电网公司 | Evaporating heat exchanger |
CN105865246A (en) * | 2016-05-31 | 2016-08-17 | 中冶焦耐工程技术有限公司 | A self-supporting corrugated straight tube heat exchange tube bundle |
CN105890407A (en) * | 2016-05-31 | 2016-08-24 | 中冶焦耐工程技术有限公司 | A self-supporting zoom tube heat exchanger and heat exchanging method |
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Publication number | Priority date | Publication date | Assignee | Title |
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US5323851A (en) * | 1993-04-21 | 1994-06-28 | Wynn's Climate Systems, Inc. | Parallel flow condenser with perforated webs |
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2003
- 2003-02-13 CN CNB031137431A patent/CN100498182C/en not_active Expired - Fee Related
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100334416C (en) * | 2004-02-10 | 2007-08-29 | 华南理工大学 | Shell and tube type heat exchanger with sharply enlarged accelerated flow zooming tube bundle and hollow ring |
CN102322768A (en) * | 2011-09-06 | 2012-01-18 | 华南理工大学 | Sugar liquid pre-heating device adopting urgent expansion accelerated flow convergent-divergent pipe internally inserted with rotational flow sheets |
CN102425973A (en) * | 2011-10-29 | 2012-04-25 | 双良节能系统股份有限公司 | Lining strip heat exchanger |
CN103267435A (en) * | 2013-06-06 | 2013-08-28 | 国家电网公司 | Evaporating heat exchanger |
CN105865246A (en) * | 2016-05-31 | 2016-08-17 | 中冶焦耐工程技术有限公司 | A self-supporting corrugated straight tube heat exchange tube bundle |
CN105890407A (en) * | 2016-05-31 | 2016-08-24 | 中冶焦耐工程技术有限公司 | A self-supporting zoom tube heat exchanger and heat exchanging method |
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