CN2809565Y - Pure countercurrent corrugated board - Google Patents

Pure countercurrent corrugated board Download PDF

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Publication number
CN2809565Y
CN2809565Y CNU2005201101472U CN200520110147U CN2809565Y CN 2809565 Y CN2809565 Y CN 2809565Y CN U2005201101472 U CNU2005201101472 U CN U2005201101472U CN 200520110147 U CN200520110147 U CN 200520110147U CN 2809565 Y CN2809565 Y CN 2809565Y
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China
Prior art keywords
plate
heat transfer
ripple
water conservancy
conservancy diversion
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Expired - Lifetime
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CNU2005201101472U
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Chinese (zh)
Inventor
张延丰
宋秉棠
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Lanzhou Petroleum Machinery Research Institute
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Individual
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    • 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
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

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  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

The utility model relates to a pure counter-flow ripple plate sheet. The utility model is characterized in that the plate sheet forms a hexagon shape; the upper part and the lower part of the plate sheet are respectively provided with a triangularly distributed flow guide region, and the middle part of the plate sheet is provided with a rectangular heat exchange region which comprises heat transfer ripples and support ripples; both sides of the plate sheet form different medium passages among the ripples; the directions of the different medium passages are opposite. The utility model has the advantages of simple structure and low cost. The utility model is used for plate type air preheaters or other air-air heat exchangers. The utility model is the pure counter-flow ripple plate sheet with different mediums, and improves the heat transfer efficiency. Support members are not needed among the plate sheets. After the plate sheets are assembled and stacked, the penetrated plate passages formed on both sides of the plate sheets have no dead area and then the utility model can realize cleaning or blowing and sweeping.

Description

Pure countercurrent corrugated board
Technical field
The utility model relates to the pure countercurrent corrugated board of the board-like heat transmitter of a kind of gas-gas, is used for the plate air preheater or other gas-gas plate type heat exchanger of combustion product gases and air heat exchange, and this plate can be realized the pure countercurrent flow of medium.
Background technology
At present, plate air preheater is a kind of advanced person's in the world an air preheater version, substitute the tubular type heat transfer element with board-like heat transfer element, adopt modes such as welding or sealing heat, solved between medium problems such as string leaks or medium leaks outside, improve the service life of equipment greatly and volume reduces greatly.Plate air preheater heat exchange element of the prior art generally is the cross-current plate, and heat transfer efficiency is low, needs to add support member between the plate, and runner such as mostly is.
Summary of the invention
The purpose of this utility model provides a kind of simple in structure, is used for the pure countercurrent corrugated board of plate air preheater or other gas-gas heat exchanger, and it improves heat transfer efficiency, does not need support member between plate.
The utility model is realized: a kind of pure countercurrent corrugated board, this plate is shaped as hexagon, its upper and lower triangle distribution water conservancy diversion district that is respectively equipped with, the centre is the rectangle heat transfer zone, described rectangle heat transfer zone is by the heat transfer ripple and support ripple, the different medium passage of the superimposed back of plate symmetry between the ripple of plate both sides formation, the different medium channel height is H and h, the different medium channel direction is opposite.
Described two ends triangle distribution water conservancy diversion district is that holding or bridging type connect with middle part rectangle heat transfer zone, angular distribution water conservancy diversion district, described two ends is mutual reversed dip corrugated plating, and passage is communicated with the same medium channel of going into, export triangle distribution water conservancy diversion district of reversed dip corrugated plating respectively between the same medium ripple of described middle part rectangle heat transfer zone.Described plate both sides different medium channel height H=h or H ≠ h.
Described heat transfer ripple is trapezoidal or S shape or triangle continuous wave pattern or interrupted ripple with supporting ripple.Described distribution water conservancy diversion district ripple is continuous or interrupted ripple.
Described distribution water conservancy diversion district is cusp or arc transition or is flat-top away from the triangular apex of rectangle heat transfer zone.
The utility model is simple in structure, does not need support member between its plate, the pure adverse current of different moving gaseouse mediums, heat transfer efficiency height.
Description of drawings
Fig. 1 is the utility model structural representation;
Fig. 2 is plate heat transfer ripple and support corrugated cross-section structural representation;
Fig. 3 is that both sides, the superimposed back of plate symmetry form the unequal generalized section of different medium channel height;
Fig. 4 is that both sides, the superimposed back of plate symmetry form the equal generalized section of different medium channel height;
The specific embodiment
Embodiment:
Shown in Fig. 1-4: a kind of pure countercurrent corrugated board, this plate is shaped as hexagon, its upper and lower triangle distribution water conservancy diversion district 1,3 that is respectively equipped with, the centre is a rectangle heat transfer zone 2, described rectangle heat transfer zone 2 comprises heat transfer ripple 201 and supports ripple 202, the different medium passage of the superimposed back of plate symmetry between the ripple of plate both sides formation, the different medium channel height is H and h, the different medium channel direction is opposite between the ripple of plate both sides.
Described two ends triangle distribution water conservancy diversion district 1,3 connects for holding or bridging type with middle part rectangle heat transfer zone 2, described angular distribution water conservancy diversion district 1,3 is mutual reversed dip corrugated plating 101, the passage same medium channel of going into, export triangle distribution water conservancy diversion district 1,3 of reversed dip corrugated plating 101 that circulates respectively between the same medium ripple of described middle part rectangle heat transfer zone 2.
Described plate both sides different medium channel height H=h or H ≠ h.
Described heat transfer ripple 201 is trapezoidal or S shape or triangle continuous wave pattern or interrupted ripple with supporting ripple 202.
Described distribution water conservancy diversion district ripple is continuous wave pattern or interrupted ripple.
Described distribution water conservancy diversion district 1 is cusp or arc transition or is flat-top away from the triangular apex of rectangle heat transfer zone 2.
Experimental results show that: following advantage is originally arranged:
1. this plate can adopt the various combination pattern, plate is made of triangle distribution water conservancy diversion district, two ends 1,3 and intermediate rectangular heat transfer zone 2 three parts, hot and cold medium B, A import rectangle heat transfer zone 2 by triangle distribution water conservancy diversion district, two ends 3,1, medium is evenly distributed along heat transfer zone 2 widths, after heat transfer zone 2 hot and cold medium B, A are pure countercurrent flow, derive by the distribution water conservancy diversion district of the other end.In order to guarantee that further homogeneous media distributes, the rectangle heat transfer zone 2 that thermal medium A enters plate by distribution water conservancy diversion district 1 one sides, and by the thermal medium A ' after the opposition side derivation heat exchange in other end distribution water conservancy diversion district 3, and the opposite side in the triangle distribution water conservancy diversion district 3 of the thermal medium A ' outflow end of cold medium B after by heat exchange enters plate rectangle heat transfer zone 2, and is derived by the triangle distribution water conservancy diversion district 1 opposition side B ' of thermal medium A upstream end.
2. the triangle distribution water conservancy diversion district 1,3 at this plate two ends and intermediate rectangular heat transfer zone 2 ripple water conservancy diversion and reinforcement heat exchange effect, and make support mutually between this plate, form the opposite side passage, need not increase other support member between the plate.
Heat transfer zone 2 plates symmetries superimposed after, the hot and cold medium B in both sides, A channel height H and h can equate or not wait, can obtain different cold and hot medium channels, as 8mm and 6mm, to adapt to different heat transfer property of cold and hot medium and mobile performance, plate air preheater (or other gas-gas heat exchanger) heat transfer efficiency and pressure drop are more optimized, adapted to the equipment enlarging demand.
4. the plate groups poststack forms passage between the plate that connects in the plate both sides, and no dead band can realize cleaning or purging.
In sum: the utility model is simple in structure, with low cost, be used for plate air preheater or other gas-gas heat exchanger, be the different medium pure countercurrent corrugated board, it improves heat transfer efficiency, does not need support member between plate, and the plate groups poststack forms passage between the plate that connects in the plate both sides, no dead band can realize cleaning or purging.

Claims (6)

1. pure countercurrent corrugated board, it is characterized in that: this plate is shaped as hexagon, its upper and lower triangle distribution water conservancy diversion district (1), (3) of being respectively equipped with, the centre is rectangle heat transfer zone (2), described rectangle heat transfer zone (2) is by heat transfer ripple (201) and support ripple (202) formation, different medium passage between the superimposed back of plate symmetry both sides formation ripple, the different medium channel height is H and h, the different medium channel direction is opposite.
2. pure countercurrent corrugated board as claimed in claim 1, it is characterized in that: described distribution water conservancy diversion district (1), (3) connect for holding or bridging type with middle part rectangle heat transfer zone (2), described upper and lower angular distribution water conservancy diversion district (1), (3) are mutual reversed dip corrugated plating (101), and passage is communicated with the same medium channel of going into, export triangle distribution water conservancy diversion district (1), (3) of reversed dip corrugated plating (101) respectively between the same medium ripple of described middle part rectangle heat transfer zone (2).
3. pure countercurrent corrugated board as claimed in claim 1 is characterized in that: the both sides different medium channel height H=h or the H ≠ h of described plate.
4. pure countercurrent corrugated board as claimed in claim 1 is characterized in that: described heat transfer ripple (201) is trapezoidal or S shape or triangle continuous wave pattern or interrupted ripple with supporting ripple (202).
5. pure countercurrent corrugated board as claimed in claim 1 is characterized in that: described distribution water conservancy diversion district ripple is continuous wave pattern or interrupted corrugated.
6. pure countercurrent corrugated board as claimed in claim 1 is characterized in that: described distribution water conservancy diversion district (1), (3) are cusp or arc transition or are flat-top away from the triangular apex of rectangle heat transfer zone (2).
CNU2005201101472U 2005-06-20 2005-06-20 Pure countercurrent corrugated board Expired - Lifetime CN2809565Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Application Number Priority Date Filing Date Title
CNU2005201101472U CN2809565Y (en) 2005-06-20 2005-06-20 Pure countercurrent corrugated board

Publications (1)

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CN2809565Y true CN2809565Y (en) 2006-08-23

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102322763A (en) * 2011-08-30 2012-01-18 南京航空航天大学 Plate type heat exchanger plate sheet with high and low staggered corrugations
CN103047892A (en) * 2013-01-31 2013-04-17 天津华赛尔传热设备有限公司 Heat transfer plate used for quadrilateral heat exchanger
CN104696983A (en) * 2015-03-12 2015-06-10 山东旺泰机械科技有限公司 Self-supporting wide gap heat exchanging element
CN104729345A (en) * 2013-12-18 2015-06-24 四平维克斯换热设备有限公司 Welded plate type heat exchanger plate
CN104729330A (en) * 2013-12-18 2015-06-24 四平维克斯换热设备有限公司 Built-in lamella heat exchanger of welding plate
CN106440868A (en) * 2015-08-13 2017-02-22 吉林省同达换热系统集成有限公司 Special-shaped capillary runner heat exchanger

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102322763A (en) * 2011-08-30 2012-01-18 南京航空航天大学 Plate type heat exchanger plate sheet with high and low staggered corrugations
CN103047892A (en) * 2013-01-31 2013-04-17 天津华赛尔传热设备有限公司 Heat transfer plate used for quadrilateral heat exchanger
CN104729345A (en) * 2013-12-18 2015-06-24 四平维克斯换热设备有限公司 Welded plate type heat exchanger plate
CN104729330A (en) * 2013-12-18 2015-06-24 四平维克斯换热设备有限公司 Built-in lamella heat exchanger of welding plate
CN104696983A (en) * 2015-03-12 2015-06-10 山东旺泰机械科技有限公司 Self-supporting wide gap heat exchanging element
CN104696983B (en) * 2015-03-12 2017-05-17 山东旺泰科技有限公司 Self-supporting wide gap heat exchanging element
CN106440868A (en) * 2015-08-13 2017-02-22 吉林省同达换热系统集成有限公司 Special-shaped capillary runner heat exchanger

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C14 Grant of patent or utility model
GR01 Patent grant
ASS Succession or assignment of patent right

Owner name: GANSU LANDTEK PETROCHEMICAL EQUIPMENT CO., LTD.

Free format text: FORMER OWNER: ZHANG YANFENG; PATENTEE

Effective date: 20080815

C41 Transfer of patent application or patent right or utility model
TR01 Transfer of patent right

Effective date of registration: 20080815

Address after: 338, Xin Wan Street, Anning District, Gansu, Lanzhou: 730070

Patentee after: Gansu blue Petrochemical Equipment Co., Ltd.

Address before: No. 349, Dunhuang Road, Qilihe District, Gansu, Lanzhou Province: 730050

Co-patentee before: Song Bingtang

Patentee before: Zhang Yan Feng

C56 Change in the name or address of the patentee

Owner name: GANSU LANDTEK PETROCHEMICAL HIGH-TECH EQUIPMENT CO

Free format text: FORMER NAME: GANSU LANDTEK PETROCHEMICAL EQUIPMENT CO., LTD.

CP03 Change of name, title or address

Address after: 338, Xin Wan Street, Anning District, Gansu, Lanzhou: 730070

Patentee after: Lanzhou Petroleum Machinery Research Institute

Address before: 338, Xin Wan Street, Anning District, Gansu, Lanzhou: 730070

Patentee before: Gansu blue Petrochemical Equipment Co., Ltd.

C17 Cessation of patent right
CX01 Expiry of patent term

Expiration termination date: 20150620

Granted publication date: 20060823