CN102322755A - Efficient rectangular pipe casing type heating network heater - Google Patents
Efficient rectangular pipe casing type heating network heater Download PDFInfo
- Publication number
- CN102322755A CN102322755A CN 201110255474 CN201110255474A CN102322755A CN 102322755 A CN102322755 A CN 102322755A CN 201110255474 CN201110255474 CN 201110255474 CN 201110255474 A CN201110255474 A CN 201110255474A CN 102322755 A CN102322755 A CN 102322755A
- Authority
- CN
- China
- Prior art keywords
- pipe
- tube
- heat
- heat exchange
- outlet
- Prior art date
- 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.)
- Pending
Links
- 238000010438 heat treatment Methods 0.000 title claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 17
- 238000005192 partition Methods 0.000 claims abstract description 5
- 230000002209 hydrophobic effect Effects 0.000 claims description 21
- 230000008676 import Effects 0.000 claims description 3
- 239000011148 porous material Substances 0.000 claims description 3
- 230000002035 prolonged effect Effects 0.000 abstract 1
- 238000007789 sealing Methods 0.000 description 4
- 230000005540 biological transmission Effects 0.000 description 3
- 238000010276 construction Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 235000014171 carbonated beverage Nutrition 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
Images
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention discloses an efficient rectangular pipe casing type heating network heater, which belongs to heat exchange equipment, in particular to small-end-difference steam and water heat exchange equipment adopting a rectangular pipe plate. The heater comprises a heater casing, a heat exchange pipe beam, a heating network circulation water inlet and an outlet, the overheat steam inlet and a drain outlet. The efficient rectangular pipe casing type heating network heater is characterized in that the heat exchange pipe beam is a rectangular heat exchange pipe beam, both sides of a front pipe plate and a back pipe plate are welded with side baffle plates, a front pipe box and a back pipe box are respectively welded at both ends of the side baffle plates, a steam inlet collection box with a steam inlet is arranged above the side baffle plates and the front and back end pipe plates, a drain collection box with the drain outlet is arranged under the side baffle plates and the front and back end pipe plates, the side baffle plate, the front and back pipe boxes, the steam inlet collection box and the drain collection box form a heater pipe casing, a circulation water inlet and the outlet are arranged on the front pipe box, and a pass partition plate is arranged in the front and back pipe boxes. The rectangular pipe plates are adopted, the space can be sufficiently utilized, the heat exchange area is increased, the length of the heat exchange pipe is short, the support is easy, the structure is simple, the steam end and the drain end can realize the small end difference, the impact on the heat exchange pipe by the steam is small, and the service life is prolonged.
Description
Technical field
The invention belongs to heat transmission equipment, particularly use the less steam-water heat exchanging equipment of end difference of rectangle tube sheet.
Background technology
Mostly its heating steam of carbonated drink heat exchangers for district heating that is used for city heat supply at present generally is superheated steam; The utilization of superheated steam generally be adopt the superheat section involucrum of sealing and feed temperature is improved reduce poor to water end (W.E.); And traditional heat exchangers for district heating becomes a unfavorable factor on the contrary owing to can not effectively utilize by the structural limitations superheated steam, makes the equipment thermal (temperature difference) stress increase and causes hidden danger; Save energy majority for the heat that utilizes steam fully simultaneously and require drain temperature low as far as possible, drain approach is less, generally about 10 degree.For realize this requirement a kind of in design be to adopt the drain cooler of connecting again, so just cause its system architecture comparatively complicated; Another kind is built-in hydrophobic cooling section just is provided with sealing in equipment a hydrophobic involucrum, so just causes the complex structure of equipment own, and thermal (temperature difference) stress take place to leak than Da Yi or hydrophobic security incident such as not smooth.For this reason, those skilled in the art were devoted in recent years to design and a kind ofly can make full use of the superheated steam degree of superheat and satisfy not only the little but also safe and practical new type heat exchanger of drain approach, but to ending at present, new breakthrough were not arranged as yet.
Summary of the invention
In order to overcome the deficiency of existing heat transmission equipment, the present invention provides a kind of high-efficiency rectangular shell-and-tube heat exchangers for district heating, and this high-efficiency rectangular shell-and-tube heat exchangers for district heating not only can make full use of the superheated steam degree of superheat, and drain approach is little, safe and practical.
The technical solution adopted for the present invention to solve the technical problems is: a kind of high-efficiency rectangular shell-and-tube heat exchangers for district heating; Comprise heater housing, heat-exchanging tube bundle, heat supply network circulating water intake, outlet; Superheated steam import, hydrophobic outlet; It is characterized in that: the rectangle heat-exchanging tube bundle that described heat-exchanging tube bundle is formed for the front end tube sheet that is welded on rectangle respectively by two ends and the heat exchanger tube of the laying of the level on the tube sheet of rear end; Tube sheet both sides, front and back are being welded side shield respectively, and semicylindrical front and back bobbin carriage is welded on the side shield two ends respectively, and the semicylindrical admission collection case that has steam inlet is equipped with in side shield and front and back end tube sheet top; The semicylindrical hydrophobic collection case that has hydrophobic outlet is equipped with in the below; Side shield, front and back bobbin carriage, admission collection case, hydrophobic collection case are formed the heater shell, and the horizontal pass partition of interlaced layout is equipped with in heat supply network circulating water intake, outlet that level is housed on the front header in the bobbin carriage of front and back.
1-2 deferent bundle support plate also is housed between the front and back tube sheet of described rectangle heat-exchanging tube bundle, and its two vertical long side is welded to connect with two side shields respectively.
Be drilled with the pore of vertical minute journey on the tube sheet of described front and back.
The air inlet below of described admission collection case is provided with the porous homogenizing plate of level.
The invention has the advantages that: thereby 1, adopt the rectangle tube sheet to make the arrangement of heat exchanger tube make full use of the space to greatest extent, under the situation in the identical space that holds heat-exchange tube, increased the quantity of heat exchanger tube, heat exchange area has been increased about 40%; 2, the support of heat exchanger tube relies on two ends tube sheet and middle tube bank support plate, has cancelled the traditional deflection plate or the supporting construction of rod baffle, and structure more simply supports more reliable; 3, recirculated water walks to manage side heat exchanger tube horizontal arrangement; Adopt the arrangement form that goes out on advancing under the short heat exchanger tube length multipaths; Steam gets into through top admission collection case, and heat exchange is flowed out by down hydrophobic collection case again through between the pipe of the uniform rectangular tube bundle in gap, with recirculated water formation countercurrent flow; 4, superheated steam also makes that to the water that is heated of low temperature thermal (temperature difference) stress is little to the condensate that is heated water low temperature of high temperature; 5, the degree of superheat of superheated steam makes full use of the superheat section involucrum that need not establish sealing and can obtain to make the effect of feed temperature raising reduction to the water end (W.E.) difference, and the hydrophobic cooling section involucrum that need not establish sealing simultaneously can obtain to reduce the effect that drain temperature is practiced thrift quantity of steam; 6, the admission space is strengthened significantly, has avoided the direct impact of steam exchange heat pipe in the prior art fully, has reduced the damage of heat exchanger tube, and the vibration of equipment, the service life of having improved equipment greatly; 7, saved a large amount of support components that use in the pipe heat exchanger, and made the simple installation of heat exchanger tube, manufacturing cost also significantly reduces; 8, the very convenient hydrophobic control of hydrophobic collection case of large space can be established drain trap no longer in addition; 9, the collection box-shaped formula of half and half cylinder type can conveniently be provided with manhole, is easy to equipment repair and maintenance, more can improve heat exchange efficiency greatly as adopting efficient heat-exchanging pipe; 10, between traditional heat exchangers vertical and horizontal between physical dimension be convenient to the installation and the layout of equipment; It is a kind of energy-efficient heat transmission equipment.
The invention has the beneficial effects as follows owing to adopt the rectangle tube sheet can make full use of the space and increase heat exchange area raising heat exchange efficiency; It is simple that heat exchanger tube length weak point is easy to supporting construction; Steam and recirculated water countercurrent flow; High-temperature steam end and hydrophobic side all can realize that the end difference is little, and employing admission collection case has increased the admission space and alleviated steam and exchange the direct impact of heat pipe and increase the service life.
Description of drawings
Fig. 1 is a structural representation of the present invention,
Fig. 2 is the A-A cutaway view of Fig. 1.
Fig. 3 is the B-B cutaway view of Fig. 1.
Among the figure, 1. front end bobbin carriage, 2. rear end bobbin carriage, 3. front end tube sheet, 4. rear end tube sheet, 5. tube bank support plate, 6. heat exchanger tube, 7. admission collection case, 8. hydrophobic collection case, 9. right side baffle plate, 10. left side baffle plate, 11. pass partitions, 12. homogenizing plates.
The specific embodiment
The specific embodiment of the present invention is, and is as shown in the figure:
1-2 deferent bundle support plate 5 also is housed between the front and back tube sheet of described rectangle heat-exchanging tube bundle, and its two vertical long side is welded to connect with two side shields respectively.
Be drilled with the pore of vertical minute journey on the tube sheet of described front and back.
The air inlet below of described admission collection case is provided with the porous homogenizing plate 12 of level.
Claims (4)
1. high-efficiency rectangular shell-and-tube heat exchangers for district heating; Comprise heater housing, heat-exchanging tube bundle, heat supply network circulating water intake, outlet; Superheated steam import, hydrophobic outlet; It is characterized in that: the rectangle heat-exchanging tube bundle that described heat-exchanging tube bundle is formed for the front end tube sheet that is welded on rectangle respectively by two ends and the heat exchanger tube of the laying of the level on the tube sheet of rear end; Tube sheet both sides, front and back are being welded side shield respectively, and semicylindrical front and back bobbin carriage is welded on the side shield two ends respectively, and the semicylindrical admission collection case that has steam inlet is equipped with in side shield and front and back end tube sheet top; The semicylindrical hydrophobic collection case that has hydrophobic outlet is equipped with in the below; Side shield, front and back bobbin carriage, admission collection case, hydrophobic collection case are formed the heater shell, and the horizontal pass partition of interlaced layout is equipped with in heat supply network circulating water intake, outlet that level is housed on the front header in the bobbin carriage of front and back.
2. high-efficiency rectangular shell-and-tube heat exchangers for district heating according to claim 1 is characterized in that: 1-2 deferent bundle support plate also is housed between the front and back tube sheet of described rectangle heat-exchanging tube bundle, and its two vertical long side is welded to connect with two side shields respectively.
3. high-efficiency rectangular shell-and-tube heat exchangers for district heating according to claim 1 is characterized in that: the pore that is drilled with vertical minute journey on the tube sheet of described front and back.
4. high-efficiency rectangular shell-and-tube heat exchangers for district heating according to claim 1 is characterized in that: the air inlet below of described admission collection case is provided with the porous homogenizing plate of level.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201110255474 CN102322755A (en) | 2011-08-31 | 2011-08-31 | Efficient rectangular pipe casing type heating network heater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201110255474 CN102322755A (en) | 2011-08-31 | 2011-08-31 | Efficient rectangular pipe casing type heating network heater |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102322755A true CN102322755A (en) | 2012-01-18 |
Family
ID=45450552
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201110255474 Pending CN102322755A (en) | 2011-08-31 | 2011-08-31 | Efficient rectangular pipe casing type heating network heater |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102322755A (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102636050A (en) * | 2012-04-27 | 2012-08-15 | 华南理工大学 | Compact type flue gas waste heat recovery heat exchanger |
| CN104132565A (en) * | 2014-06-30 | 2014-11-05 | 广东中蓝能源环保产业有限公司 | Waste gas afterheat recovery heat exchanger |
| CN105972826A (en) * | 2016-05-19 | 2016-09-28 | 佛山市晟恺热能设备有限公司 | Water-cooled low-nitric-oxide heat exchanger |
| CN106247814A (en) * | 2016-07-20 | 2016-12-21 | 杭州佰强能源科技有限公司 | A kind of water and vapor heat exchanger and heat-exchange system |
| EP3021065A4 (en) * | 2013-07-12 | 2017-04-19 | Cordón Urbiola, Jose, Luis | Heat recovery unit |
| CN106595043A (en) * | 2016-12-14 | 2017-04-26 | 阳谷祥光铜业有限公司 | Gas heating device |
| CN107816903A (en) * | 2016-09-11 | 2018-03-20 | 郎风 | Baffled multipass heat exchanger |
| CN109505805A (en) * | 2018-12-29 | 2019-03-22 | 广东焕能科技有限公司 | A kind of centrifugal air compressor heat-exchange system |
| CN110230934A (en) * | 2019-07-01 | 2019-09-13 | 扬中申扬换热设备有限公司 | A kind of shell-and-tube heat exchanger |
| CN118856946A (en) * | 2023-11-08 | 2024-10-29 | 山东大学 | A vertical heat exchanger with a straight flow plate |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201867091U (en) * | 2010-11-12 | 2011-06-15 | 山东北辰压力容器有限公司 | Rectangular all-welded tube and shell type heater for heating network |
-
2011
- 2011-08-31 CN CN 201110255474 patent/CN102322755A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201867091U (en) * | 2010-11-12 | 2011-06-15 | 山东北辰压力容器有限公司 | Rectangular all-welded tube and shell type heater for heating network |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102636050A (en) * | 2012-04-27 | 2012-08-15 | 华南理工大学 | Compact type flue gas waste heat recovery heat exchanger |
| EP3021065A4 (en) * | 2013-07-12 | 2017-04-19 | Cordón Urbiola, Jose, Luis | Heat recovery unit |
| CN104132565A (en) * | 2014-06-30 | 2014-11-05 | 广东中蓝能源环保产业有限公司 | Waste gas afterheat recovery heat exchanger |
| CN104132565B (en) * | 2014-06-30 | 2016-08-17 | 广东中蓝能源环保产业有限公司 | Waste gas residual heat recovery heat exchanger |
| CN105972826A (en) * | 2016-05-19 | 2016-09-28 | 佛山市晟恺热能设备有限公司 | Water-cooled low-nitric-oxide heat exchanger |
| CN106247814A (en) * | 2016-07-20 | 2016-12-21 | 杭州佰强能源科技有限公司 | A kind of water and vapor heat exchanger and heat-exchange system |
| CN107816903A (en) * | 2016-09-11 | 2018-03-20 | 郎风 | Baffled multipass heat exchanger |
| CN106595043A (en) * | 2016-12-14 | 2017-04-26 | 阳谷祥光铜业有限公司 | Gas heating device |
| CN109505805A (en) * | 2018-12-29 | 2019-03-22 | 广东焕能科技有限公司 | A kind of centrifugal air compressor heat-exchange system |
| CN110230934A (en) * | 2019-07-01 | 2019-09-13 | 扬中申扬换热设备有限公司 | A kind of shell-and-tube heat exchanger |
| CN118856946A (en) * | 2023-11-08 | 2024-10-29 | 山东大学 | A vertical heat exchanger with a straight flow plate |
| CN118856946B (en) * | 2023-11-08 | 2025-04-29 | 山东大学 | Vertical heat exchanger with straight-line flow equalization plates |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102322755A (en) | Efficient rectangular pipe casing type heating network heater | |
| CN202254970U (en) | Efficient rectangular shell-and-tube heating network heater | |
| CN204806941U (en) | Heat exchanger | |
| CN104864747A (en) | Energy-saving heating network heater | |
| CN104913672A (en) | Box type shell and tube heat exchanger | |
| CN105571354B (en) | Flue gas waste heat recovery apparatus and flue gas waste heat recovery method based on double-U-shaped shell-and-tube heat exchanger | |
| CN102878673B (en) | Oil-gas organic heat transfer furnace | |
| CN104930882A (en) | U-shaped pipe energy-saving heater for heating network | |
| CN201867091U (en) | Rectangular all-welded tube and shell type heater for heating network | |
| CN203628620U (en) | Reinforced composite phase change heat exchanger | |
| CN105333753A (en) | Efficient heat exchanger | |
| CN202002514U (en) | Self-expansion low-temperature draining type heating network heater | |
| CN103574569B (en) | cement kiln head waste heat boiler | |
| CN111780420A (en) | Main heat exchanger of wall-mounted boiler | |
| CN202973973U (en) | Overall expansion type heater for heating network | |
| CN211902837U (en) | Structure for overheating top and cladding of horizontal flue of waste incineration waste heat boiler | |
| CN201476612U (en) | Shell heat exchanger | |
| CN204787950U (en) | Box shell and tube type heat exchanger | |
| CN104457338A (en) | Heat exchanging method for horizontal type heat exchanger for steam cooling with high degree of superheat | |
| CN205448762U (en) | Water storage formula stainless steel heat exchanger | |
| CN202547448U (en) | Heat exchanger for smoke waste heat recovery | |
| CN203719481U (en) | Economizer of boiler heat exchange system | |
| CN201811622U (en) | Radial heat pipe heat exchanger | |
| CN111207385A (en) | Horizontal flue furnace top and cladding overheating structure of waste incineration waste heat boiler | |
| CN117128530B (en) | Heat pipe type flue gas heating fused salt heat storage system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C53 | Correction of patent for invention or patent application | ||
| CB02 | Change of applicant information |
Address after: 250305 No. 6 Beichen Road, five mountain tourism resort, Changqing District, Shandong, Ji'nan Applicant after: Shandong Beichen Electromechanical Device Co., Ltd. Address before: 250305 No. 6 Beichen Road, five mountain tourism resort, Changqing District, Shandong, Ji'nan Applicant before: Shandong Beichen Pressure Vessel Co., Ltd. |
|
| COR | Change of bibliographic data |
Free format text: CORRECT: APPLICANT; FROM: SHANDONG BEICHEN PRESSURE VESSEL CO., LTD. TO: SHANDONG BEICHEN ELECTROMECHANICAL EQUIPMENT CO., LTD. |
|
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20120118 |