CN2527953Y - Film-type wall-type heat-exchanger for desulfurization - Google Patents

Film-type wall-type heat-exchanger for desulfurization Download PDF

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Publication number
CN2527953Y
CN2527953Y CN 02219267 CN02219267U CN2527953Y CN 2527953 Y CN2527953 Y CN 2527953Y CN 02219267 CN02219267 CN 02219267 CN 02219267 U CN02219267 U CN 02219267U CN 2527953 Y CN2527953 Y CN 2527953Y
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China
Prior art keywords
seamless steel
steel pipe
ratio
steel tube
seamless
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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
CN 02219267
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Chinese (zh)
Inventor
王立群
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Jiangsu University
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Jiangsu University
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Priority to CN 02219267 priority Critical patent/CN2527953Y/en
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Publication of CN2527953Y publication Critical patent/CN2527953Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

Disclosed is a film and wall desulfurizing heat exchanger used in flue gas desulfurization. A wing panel is arranged outside a seamless steel tube and along an axle, and is connected with a neighboring steel tube. A bundle of seamless steel tubes is connected with the wing panel to form a film wall along a steel tube axle. The bundle of seamless steel tubes can be arranged in parallel, staggered, or in sequence. The ratio of the lateral space S1 between seamless steel tubes versus the external diameter (d) of a seamless steel tube equals to 2.0 to 3.0; the ratio of the vertical space S2 versus the external diameter (d) of the seamless steel tube equals to 1.0 to 2.0; the ratio of (d) of the seamless steel tube versus the thickness (t) of the wing panel equals to 9.5 to 16. Since dust is unsusceptible to deposit on the film wall, the corrosion of seamless tubes and the wing panel is greatly slowed down. Consequently, the ventilation resistance is reduced and the heat transmission efficiency is strengthened.

Description

Membrane type wall type desulfurization heat exchanger
Technical field
The utility model relates to energy device, refers in particular to a kind of membrane type wall type desulfurization heat exchanger that is used for flue gas desulfur device.
Background technology
At present, along with the continuous reinforcement of environmental requirement, thermal power plant and boiler equipment all have dust-removing desulfurating apparatus.The desulfur technology of existing extensive use is lime stone (lime) gypsum wet flue gas desulfurizing method, and the cooling heat exchanger in order to reduce flue-gas temperature before the desulfurization is one of key equipment wherein, and its general spiral-finned tube that adopts is made heat exchange element now.Because the thermograde of heat exchanger is big, and heat exchanger exit place cigarette temperature has been lower than the dew-point temperature of flue gas, a large amount of SO 2And SO 3Easily form sulfuric acid, thereby form cement-like material, spiral-finned tube is blocked based on calcium sulfate with flying dust in the flue gas in the tube bank surface condensation, very difficult during cleaning, dust stratification causes heat transfer resistance sharply to increase simultaneously, and flowing resistance increases, and has quickened the corrosion of tube wall.
Summary of the invention
The purpose of this utility model is that a kind of heat transfer efficiency height will be provided, the membrane type wall type desulfurization heat exchanger of job stability and good endurance.
Its objective is such realization:
It has seamless steel pipe, it is characterized in that the seamless steel pipe outer is axially arranged with the fin that connects adjacent steel pipe, the seamless steel pipe bundle with fin link to each other form along steel shaft to membrane wall.
Seamless steel pipe Shu Caiyong is arranged in parallel, stagger arrangement, all can along row.Horizontal spacing S between seamless steel pipe 1Equal 2.0~3.0, longitudinal pitch S with the ratio of seamless steel pipe outside diameter d 2Equal 1.2~2.0 with the ratio of seamless steel pipe outside diameter d, seamless steel pipe d equals 9.5~16 with the ratio of the thickness t of fin.
Advantage of the present utility model is to adopt seamless steel pipe to link to each other with longitudinal fin and forms membrane wall structure, in the time of can guaranteeing when heat exchanger is worked the passage between wet every layer of membrane wall of dirt airflow passes, wet ash does not have obvious stagnant wake at the seamless steel pipe afterbody, therefore, wet ash is difficult for amassing on tube wall, but is taken away by the air-flow of certain flow rate.Heat exchanger is owing to be difficult for dust stratification like this, and the corrosion that has slowed down seamless steel pipe and fin has greatly reduced flowing resistance, has strengthened heat transfer efficiency.
Description of drawings
Fig. 1 is a structural representation of the present utility model
Embodiment
As shown in the figure, the utlity model has seamless steel pipe 1, outside along laterally being provided with fin 2 at it, and the interbank fin of each layer interconnect through seamless steel pipe, forms membrane wall with steel pipe.The seamless steel pipe bundle adopts up and down and is arranged in parallel, its horizontal spacing S 1, with the ratio of seamless steel pipe outside diameter d be 2.5, longitudinal pitch S 2With the ratio of seamless steel pipe outside diameter d be 1.2~2.0, seamless steel pipe d is 9.5~16 with the ratio of the thickness t of fin.Tube bank also can be adopted along row and arrange.

Claims (3)

1, membrane type wall type desulfurization heat exchanger, it has seamless steel pipe, it is characterized in that seamless steel pipe (1) outer is axially arranged with the fin (2) that connects adjacent steel pipe, seamless steel pipe bundle (1) with fin (2) link to each other formation along steel shaft to membrane wall.
2, membrane type wall type desulfurization heat exchanger according to claim 1 is characterized in that seamless steel pipe Shu Caiyong is arranged in parallel, stagger arrangement, all can along row.
3, membrane type wall type desulfurization heat exchanger according to claim 1 is characterized in that the horizontal spacing S between seamless steel pipe 1Equal 2.0~3.0, longitudinal pitch S with the ratio of seamless steel pipe outside diameter d 2Equal 1.2~2.0 with the ratio of seamless steel pipe outside diameter d, seamless steel pipe d equals 9.5~16 with the ratio of the thickness t of fin.
CN 02219267 2002-03-12 2002-03-12 Film-type wall-type heat-exchanger for desulfurization Expired - Fee Related CN2527953Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 02219267 CN2527953Y (en) 2002-03-12 2002-03-12 Film-type wall-type heat-exchanger for desulfurization

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 02219267 CN2527953Y (en) 2002-03-12 2002-03-12 Film-type wall-type heat-exchanger for desulfurization

Publications (1)

Publication Number Publication Date
CN2527953Y true CN2527953Y (en) 2002-12-25

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN 02219267 Expired - Fee Related CN2527953Y (en) 2002-03-12 2002-03-12 Film-type wall-type heat-exchanger for desulfurization

Country Status (1)

Country Link
CN (1) CN2527953Y (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101266113B (en) * 2007-03-15 2011-05-25 财团法人工业技术研究院 Water heater and its heat converter structure
CN102374791A (en) * 2010-08-06 2012-03-14 烟台鑫丰源电站设备有限公司 Waste heat recovery device for industrial furnace waste gas or coal gas
CN101762157B (en) * 2008-10-27 2012-11-14 中国恩菲工程技术有限公司 Metallurgical furnace
CN108167800A (en) * 2017-12-25 2018-06-15 浙江浙能技术研究院有限公司 A kind of improvement boiler economizer

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101266113B (en) * 2007-03-15 2011-05-25 财团法人工业技术研究院 Water heater and its heat converter structure
CN101762157B (en) * 2008-10-27 2012-11-14 中国恩菲工程技术有限公司 Metallurgical furnace
CN102374791A (en) * 2010-08-06 2012-03-14 烟台鑫丰源电站设备有限公司 Waste heat recovery device for industrial furnace waste gas or coal gas
CN108167800A (en) * 2017-12-25 2018-06-15 浙江浙能技术研究院有限公司 A kind of improvement boiler economizer

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GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee