CN103837024A - Low fin type heat exchanger - Google Patents

Low fin type heat exchanger Download PDF

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Publication number
CN103837024A
CN103837024A CN201210484312.5A CN201210484312A CN103837024A CN 103837024 A CN103837024 A CN 103837024A CN 201210484312 A CN201210484312 A CN 201210484312A CN 103837024 A CN103837024 A CN 103837024A
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CN
China
Prior art keywords
low
heat exchange
exchange pipe
heat exchanger
deflection plate
Prior art date
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Pending
Application number
CN201210484312.5A
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Chinese (zh)
Inventor
莫顺才
陈亦平
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.)
YIXING HUIFU MACHINERY EQUIPMENT CO Ltd
Original Assignee
YIXING HUIFU MACHINERY EQUIPMENT CO Ltd
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 YIXING HUIFU MACHINERY EQUIPMENT CO Ltd filed Critical YIXING HUIFU MACHINERY EQUIPMENT CO Ltd
Priority to CN201210484312.5A priority Critical patent/CN103837024A/en
Publication of CN103837024A publication Critical patent/CN103837024A/en
Pending legal-status Critical Current

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Abstract

The invention discloses a low fin type heat exchanger comprising a tube body and low fin type heat exchange tubes. Channels are arranged at the two ends of the tube body respectively, and a lug type support, a heat source inlet and a cold source outlet are formed in the side wall of the tube body. The channel close to the cold source outlet is provided with a material inlet, and the channel close to the heat source inlet is provided with a material outlet. The low fin type heat exchange tubes are connected through tube sheets and supported through baffle plates arrayed at intervals. The baffle plates are fixed through pull rods arrayed at intervals. The tube sheets are welded to the tube body, and the channels are connected with the tube body through flanges. The low fin type heat exchange tubes are adopted as heat exchange elements, so that the heat exchange area is large, meanwhile, when media flow through the surfaces of the low fin type heat exchange tubes, fins has a turbulence effect on the edge layers of laminar flows to form surface turbulent flows, and a good heat exchange effect is achieved; the low fin type heat exchange tubes are low, so that tube penetrating is convenient, flow resistance is small, differential pressure is low, needed power is low, the fin distance is reasonable, and the heat transfer effect is good.

Description

Low finned heat exchanger
Technical field
The invention belongs to technical field of heat exchange, relate to low finned heat exchanger, be specifically related to a kind of efficient low finned heat exchanger.
Background technology
Heat exchanger is mainly used in the exchange heat of chemical industry, pharmaceutical industry, environment-friendly engineering industry, present most of heat exchanger uses light pipe as heat exchanger tube, because light pipe does not have perturbation action to heat-transfer fluid, heat-transfer fluid flows steadily, heat transfer efficiency is general, under identical heat exchange area condition, former heat exchanger area occupied is larger, and required heat source fluid is more.
Summary of the invention
Object of the present invention solves the deficiencies in the prior art, and a kind of efficient low finned heat exchanger is provided.
Object of the present invention can be achieved through the following technical solutions:
A kind of low finned heat exchanger, comprise cylindrical shell and low fin heat exchange pipe, described cylindrical shell two ends are respectively equipped with bobbin carriage, and cylinder lateral wall is provided with hanging support, thermal source import and low-temperature receiver outlet, bobbin carriage near low-temperature receiver outlet is provided with material inlet, is provided with material outlet near the bobbin carriage of thermal source import; Described low fin heat exchange pipe connects by tube sheet, and low fin heat exchange pipe is supported by spaced deflection plate, and deflection plate is fixed by spaced pull bar; Described Tube-sheet Welding is on cylindrical shell, and bobbin carriage is connected by flange seal with cylindrical shell.
Described low finned heat exchanger, also comprises stainless steel lining ring and rivet, and described stainless steel lining ring is arranged on the gap location of deflection plate and cylindrical shell, described stainless steel lining ring and deflection plate lap rivet rivet welding.
The thickness of described stainless steel lining ring is 0.5mm.
Described stainless steel lining ring and the lap width of deflection plate are 20~30mm.
Described deflection plate is circular arc plate, is provided with and is the circular hole that equilateral triangle distributes, and is convenient to pull bar and low fin heat exchange pipe poling.
Described low fin heat exchange pipe forms screw thread fin in the rolling of light pipe outer surface, and low fin heat exchange pipe diameter is 19~38mm, and fin height is 0.5~2.0mm, and a pitch of fins is 1.0~3.0mm.
Described low fin heat exchange pipe adopts sizing rolling.
Described low fin heat exchange pipe is leaving 20mm light pipe with deflection plate intersection, and between light pipe and deflection plate, gap is 0.2~0.4mm.
Described low fin heat exchange pipe and tube sheet are connected by expanded joint, welding or expanded and welded tube joint and by mode.
Orthogonal between described deflection plate and pull bar.
Beneficial effect of the present invention:
1, the present invention adopts low fin heat exchange pipe to make heat exchange element, and hot expansibility is good, has larger heat exchange area under same size, shell side MEDIA FLOW is in the time of low fin heat exchange pipe surface simultaneously, fin produces flow-disturbing effect to laminar flow boundary layer, forms turbulent surface flow, has higher heat transfer effect.
2, the setting of low fin heat exchange pipe fin is lower, is convenient to poling, and fluid resistance is less, and pressure drop is lower, and required drive is less, and a pitch of fins arranges rationally, and heat-transfer effect is good.
Brief description of the drawings
Fig. 1 is structural representation of the present invention.
In Fig. 1,1-cylindrical shell, 2-material inlet, 3-bobbin carriage, 4-flange, 5-tube sheet, 6-deflection plate, the low fin heat exchange pipe of 7-, 8-hanging support, the import of 9-thermal source, 10-pull bar, 11-bobbin carriage, 12-material outlet, the outlet of 13-low-temperature receiver.
Fig. 2 is deflection plate of the present invention and stainless steel lining ring connection layout.
In Fig. 2,6-deflection plate, 14-stainless steel lining ring, 15-rivet.
Fig. 3 is the enlarged drawing of low fin heat exchange pipe.
In Fig. 3, the low fin heat exchange pipe of 7-, 7.1-fin, 7.2-light pipe.
Detailed description of the invention
Below with reference to the accompanying drawings and in conjunction with the embodiments, the present invention will be further described.
Low finned heat exchanger shown in Fig. 1 is a kind of vertical heat exchanger, comprise cylindrical shell 1 and low fin heat exchange pipe 7, described cylindrical shell 1 two ends are respectively equipped with bobbin carriage, cylinder lateral wall is provided with hanging support 8, thermal source import 9 and low-temperature receiver outlet 13, bobbin carriage 3 near low-temperature receiver outlet 13 is provided with material inlet 2, is provided with material outlet (12) near the bobbin carriage 11 of thermal source import 9; Described low fin heat exchange pipe 7 connects by tube sheet 5, and low fin heat exchange pipe 7 is supported by spaced deflection plate 6, and deflection plate 6 is fixing by spaced pull bar 10; Described tube sheet 5 is welded on cylindrical shell 1, and bobbin carriage and cylindrical shell 1 are tightly connected by flange 4.
Described low finned heat exchanger, also comprises stainless steel lining ring 14 and rivet 15, and described stainless steel steel ring is arranged on the gap location of deflection plate and cylindrical shell, described stainless steel lining ring 14 and deflection plate rivet 15 rivet weldings for 6 laps.
The thickness of described stainless steel lining ring 14 is 0.5mm.
Described stainless steel lining ring 14 and the lap width of deflection plate 6 are 20~30mm.
Described deflection plate 6 is circular arc plate, is provided with and is the circular hole that equilateral triangle distributes, and is convenient to pull bar and low fin heat exchange pipe poling.
The screw thread fin that described low fin heat exchange pipe 7 forms in the rolling of light pipe outer surface, low fin heat exchange pipe diameter is 19~38mm, and fin height is 0.5~2.0mm, and a pitch of fins is 1.0~3.0mm.Described low fin heat exchange pipe adopts sizing rolling.
Described low fin heat exchange pipe 7 is leaving 20mm light pipe with deflection plate 6 intersections, and between light pipe and deflection plate, gap is 0.2~0.4mm.
Described low fin heat exchange pipe 7 and tube sheet 5 are connected by expanded joint, welding or expanded and welded tube joint and by mode.
Orthogonal between described deflection plate 6 and pull bar 10.
The present invention adopts low fin heat exchange pipe to make heat exchange element, and hot expansibility is good, has larger heat exchange area under same size, shell side MEDIA FLOW is in the time of low fin heat exchange pipe surface simultaneously, fin produces flow-disturbing effect to laminar flow boundary layer, forms turbulent surface flow, has higher heat transfer effect; The setting of low fin heat exchange pipe fin is lower, is convenient to poling, and fluid resistance is less, and pressure drop is lower, and required drive is less, and a pitch of fins arranges rationally, and heat-transfer effect is good.

Claims (6)

1. a low finned heat exchanger, it is characterized in that: comprise cylindrical shell (1) and low fin heat exchange pipe (7), described cylindrical shell (1) two ends are respectively equipped with bobbin carriage, cylinder lateral wall is provided with hanging support (8), thermal source import (9) and low-temperature receiver outlet (13), bobbin carriage (3) near low-temperature receiver outlet (13) is provided with material inlet (2), is provided with material outlet (12) near the bobbin carriage (11) of thermal source import (9); Described low fin heat exchange pipe (7) connects by tube sheet (5), low fin heat exchange pipe (7) is supported by spaced deflection plate (6), and deflection plate (6) is fixing by spaced pull bar (10); It is upper that described tube sheet (5) is welded on cylindrical shell (1), and bobbin carriage and cylindrical shell (1) are tightly connected by flange (4).
2. low finned heat exchanger according to claim 1, characterized by further comprising stainless steel lining ring (14) and rivet (15), described stainless steel lining ring (14) is arranged on gap location, described stainless steel lining ring (14) and deflection plate (6) rivet for lap (15) rivet welding of deflection plate (6) and cylindrical shell (1).
3. low finned heat exchanger according to claim 2, the thickness that it is characterized in that described stainless steel lining ring (14) is 0.5mm, and described stainless steel lining ring (14) and the lap width of deflection plate (6) are 20~30mm.
4. low finned heat exchanger according to claim 1, it is characterized in that described low fin heat exchange pipe (7) forms screw thread fin (7.1) in the rolling of light pipe outer surface, low fin heat exchange pipe diameter is 19~38mm, fin height is 0.5~2.0mm, and a pitch of fins is 1.0~3.0mm.
5. low finned heat exchanger according to claim 1, is characterized in that described low fin heat exchange pipe (7) is leaving 20mm light pipe (7.2) with deflection plate (6) intersection.
6. low finned heat exchanger according to claim 1, is characterized in that described low fin heat exchange pipe (7) and tube sheet (5) are connected by expanded joint, welding or expanded and welded tube joint and by mode.
CN201210484312.5A 2012-11-23 2012-11-23 Low fin type heat exchanger Pending CN103837024A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201210484312.5A CN103837024A (en) 2012-11-23 2012-11-23 Low fin type heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201210484312.5A CN103837024A (en) 2012-11-23 2012-11-23 Low fin type heat exchanger

Publications (1)

Publication Number Publication Date
CN103837024A true CN103837024A (en) 2014-06-04

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CN (1) CN103837024A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105004207A (en) * 2015-07-01 2015-10-28 太仓市顺邦防腐设备有限公司 Compound corrosion resisting heat exchanger
CN105091635A (en) * 2015-08-11 2015-11-25 江苏永大化工机械有限公司 Novel efficient heat exchanger
CN108568964A (en) * 2018-04-12 2018-09-25 宁夏金梯氟塑防腐设备有限公司 Steel lining tetrafluoro ethylene pipe processing device
CN111220009A (en) * 2020-01-16 2020-06-02 沂州科技有限公司 Low-temperature heat pipe evaporator for coke oven flue gas waste heat recovery system

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2713471A (en) * 1970-04-23 1972-10-05 Borgwarner Corporation Baffle for shelland tube heat exchangers
US4834173A (en) * 1987-11-20 1989-05-30 American Standard Inc. Pressure actuated baffle seal
CN101975522A (en) * 2010-11-09 2011-02-16 上海化工研究院 High-efficient heat exchanger
JP2011117656A (en) * 2009-12-02 2011-06-16 Tokyo Titanium Co Ltd Shell and tube heat exchanger
CN202255024U (en) * 2011-09-17 2012-05-30 西安优耐特容器制造有限公司 Finned tube with external threads and internal spiral grooves
CN203011202U (en) * 2012-11-23 2013-06-19 宜兴市汇富机械设备有限公司 Low fin heat exchanger

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2713471A (en) * 1970-04-23 1972-10-05 Borgwarner Corporation Baffle for shelland tube heat exchangers
US4834173A (en) * 1987-11-20 1989-05-30 American Standard Inc. Pressure actuated baffle seal
JP2011117656A (en) * 2009-12-02 2011-06-16 Tokyo Titanium Co Ltd Shell and tube heat exchanger
CN101975522A (en) * 2010-11-09 2011-02-16 上海化工研究院 High-efficient heat exchanger
CN202255024U (en) * 2011-09-17 2012-05-30 西安优耐特容器制造有限公司 Finned tube with external threads and internal spiral grooves
CN203011202U (en) * 2012-11-23 2013-06-19 宜兴市汇富机械设备有限公司 Low fin heat exchanger

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105004207A (en) * 2015-07-01 2015-10-28 太仓市顺邦防腐设备有限公司 Compound corrosion resisting heat exchanger
CN105091635A (en) * 2015-08-11 2015-11-25 江苏永大化工机械有限公司 Novel efficient heat exchanger
CN108568964A (en) * 2018-04-12 2018-09-25 宁夏金梯氟塑防腐设备有限公司 Steel lining tetrafluoro ethylene pipe processing device
CN108568964B (en) * 2018-04-12 2023-12-22 宁夏金梯氟塑防腐设备有限公司 Steel lining tetrafluoroethylene pipe processing device
CN111220009A (en) * 2020-01-16 2020-06-02 沂州科技有限公司 Low-temperature heat pipe evaporator for coke oven flue gas waste heat recovery system

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Application publication date: 20140604