CN205049023U - Tubular heat exchange energy conservation device - Google Patents

Tubular heat exchange energy conservation device Download PDF

Info

Publication number
CN205049023U
CN205049023U CN201520751406.3U CN201520751406U CN205049023U CN 205049023 U CN205049023 U CN 205049023U CN 201520751406 U CN201520751406 U CN 201520751406U CN 205049023 U CN205049023 U CN 205049023U
Authority
CN
China
Prior art keywords
bearing
fixed
heat exchange
heat transfer
support
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.)
Expired - Fee Related
Application number
CN201520751406.3U
Other languages
Chinese (zh)
Inventor
赵彦成
黄忠军
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.)
Jiangsu high energy saving Technology Co., Ltd.
Original Assignee
赵彦成
黄忠军
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 赵彦成, 黄忠军 filed Critical 赵彦成
Priority to CN201520751406.3U priority Critical patent/CN205049023U/en
Application granted granted Critical
Publication of CN205049023U publication Critical patent/CN205049023U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The utility model discloses a tubular heat exchange energy conservation device, including spacing support, fixed bolster, bearing retainer, bearing, spiral tie, fixed axle and fixed pin, the inside spiral tie that is equipped with of tubular heat exchange tube, the fixed axle is connected to the spiral tie, is equipped with the bearing on the fixed axle, and the bearing is inlayed on bearing retainer, and bearing retainer fixes on spacing support, spacing leg joint fixed bolster, the fixed bolster is fixed on the heat exchanger end plate. Compared with the prior art, the utility model discloses heat exchange efficiency is higher, and energy waste subtracts still less, can reach the purpose of energy saving and emission reduction consumption reduction, can at every moment clear away the incrustation scale of heat exchange tube inner wall, makes the heat exchange tube be in the optimum condition of heat transfer all the time.

Description

Pipe type heat transfer energy saver
Technical field
The utility model relates to field of energy-saving technology, is specifically related to pipe type heat transfer energy saver.
Background technology
Pipe heat exchanger, it is most typical dividing wall type heat exchanger, and its application industrially has long history, and still dominate in all heat exchangers so far.Pipe heat exchanger mainly contains housing, tube bank, tube sheet and envelope first class sections composition, and how rounded housing is, and bundle of parallel tubes is equipped with in inside, and tube bank two ends are fixed on end plate.Pipe heat exchanger is difficult to thorough cleaning because of its special tubular structure, the heat exchange efficiency of pipe heat exchanger is caused to decline, energy consumption promotes, and impact and the removing technique of most enterprises and individual heat exchanging equipment fouling also rest on traditional " destructiveness " technique and the idea aspects such as machinery, water under high pressure, chemical pickling; Therefore be necessary to design a set of simple, safe, effective, easy-operating cleaning model to pipe heat exchanger.
In prior art, carry out two kinds of fluids of heat exchange in pipe heat exchanger, a kind of at Bottomhole pressure, a kind of in the outer flowing of pipe, the wall of tube bank is heat-transfer area.For improving extratubal fluid heat transfer coefficient, the horizontal baffle plate of some is installed in housing usually.Baffle plate not only can anti-fluid short circuit, increases fluid velocity, also force fluid by prescribed path repeatedly cross-flow by tube bank, less turbulence is greatly increased.And the medium flowed in pipe heat exchanger mostly is water, and the very easily fouling of this medium of water, the thickness that incrustation scale is attached to tube wall is thicker, the heat transfer effect of pipe heat exchanger is poorer, energy consumption is finally caused to rise, because pipe heat exchanger mostly is closed, cleaning is comparatively complicated, and traditional Chemical cleaning water treating method is the water treatment agent adding 3 kinds of not same-actions: corrosion inhibiter, antisludging agent and Biocidal algae-killing agent.Corrosion inhibiter can form epithelium in metal surface, prevents corrosion; Antisludging agent acts on the crystalline solid of the composition calcium carbonate forming dirt etc., makes its distortion, dislocation, distortion, hinders the growth of dirt with this; Biocidal algae-killing agent has inhibitory action to algea and bacteria, prevents it from breeding.Water Treatment method can reach good effect in theory, prerequisite is effective water quality stabilizer, professional operation and management and responsible operating personnel, due to above situation and feature, the effect often poor effect of Water Treatment, incrustation scale is assembled gradually again after bubble disclosed by hairbrush.Even if so current most of air conditioning cooling water system takes chemical water treatment method, also want during annual maintenance downtime in winter, to adopt hairbrush to disclose bubble cleaning condenser simultaneously, the copper pipe of pipe heat exchanger is not only straight but also long, particularly tubular heat exchanger, the condenser of such as central air conditioner main machine and evaporimeter, when current flow through Straight Pipes of Heat Exchanger, due to the existence of frictional resistance, and can not eliminate, no matter which kind of state current are in, the closer to the limit wall of tube wall, the flow velocity of water is slower, namely our laminar flow layer of often saying, the thickness of laminar flow layer depends on the flow velocity of pipeline, flow velocity is faster, laminar sublayer is thinner, the heat transfer type of laminar sublayer is generally conduction heat transfer, heat transfer efficiency is far below the convection heat transfer' heat-transfer by convection in centre, therefore the thickness increase heat exchange efficiency of reduction layer laminar sublayer is just extremely important!
The shortcoming and defect of prior art is, pipe heat exchanger is difficult to thorough cleaning because of its special tubular structure, the impact of most enterprises and individual heat exchanging equipment fouling and remove technique and also rest on traditional " destructiveness " technique and the idea aspects such as machinery, water under high pressure, chemical pickling; And think that equipment cleaning only just can be considered when having a strong impact on equipment and running simply, what it did not know incrustation scale is created on the energy consumption constantly affecting enterprise, engulfs the profit of enterprise.And the single expense in order to reduce cleaning, have selected cleaning method equipment being had to infringement and corrosion, causes the stagnation of scrapping and producing of equipment, paid than energy saver high the hundred times even cost of thousands of times.A lot of enterprise at present; adopt oxalic acid cleaning heat transmission equipment; each scavenging period all dare not more than two hours; thorough not because of what clean; so scavenging period from before become present 1 year three times annually; add the shutdown off-time of twice, indirectly cause loss to enterprise, and the waste water and waste liquid after cleaning causes great infringement to environment again.
Summary of the invention
It is high that the purpose of this utility model is to provide a kind of heat exchange efficiency, energy waste reduces, the object of energy-saving and emission-reduction consumption reduction can be reached, the incrustation scale of heat exchanger tube inwall can be removed momently, make heat exchanger tube be in the pipe type heat transfer energy saver of the optimum condition of heat exchange all the time.
For achieving the above object, the utility model provides following technical scheme:
Pipe type heat transfer energy saver, comprise limiting bracket, fixed support, the support of bearing, bearing, spiral band, fixed axis and steady pin, pipe type heat transfer pipe inside is provided with spiral band, spiral band is connected and fixed axle, fixed axis is provided with bearing, and bearing is embedded on the support of bearing, and the support of bearing is fixed on limiting bracket, limiting bracket is connected and fixed support, and fixed support is fixed on heat exchanger end plate.
As the further improvement of above-mentioned technology, described spiral band is connected and fixed axle by steady pin.
As the further improvement of above-mentioned technology, described steady pin adopts riveting method to connect spiral band and fixed axis.
As the further improvement of above-mentioned technology, described limiting bracket is by being welded to connect fixed support.
As the further improvement of above-mentioned technology, described limiting bracket, fixed support, the support of bearing, fixed axis, steady pin, bearing all adopt food-grade 304 stainless steel to customize and form.
As the further improvement of above-mentioned technology, described spiral band adopts the customization of high molecular nanometer material to form.
Compared with prior art, the beneficial effects of the utility model are: improve heat exchange efficiency, reduce energy waste, reach the object of energy-saving and emission-reduction consumption reduction, can remove the incrustation scale of heat exchanger tube inwall momently, make heat exchanger tube be in the optimum condition of heat exchange all the time, heat exchange efficiency improves about 30%.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure: 1: limiting bracket; 2: fixed support; 3: the support of bearing; 4: bearing; 5: spiral band; 6: pipe type heat transfer pipe; 7: fixed axis; 8: steady pin; 9: heat exchanger end plate.
Detailed description of the invention
Be described in more detail below in conjunction with the technical scheme of detailed description of the invention to this patent.
Pipe type heat transfer energy saver, comprise limiting bracket 1, fixed support 2, the support of bearing 3, bearing 4, spiral band 5, fixed axis 7 and steady pin 8, pipe type heat transfer pipe 6 inside is provided with spiral band 5, spiral band 5 adopts riveting method to be connected and fixed axle 7 by steady pin 8, fixed axis 7 is provided with bearing 4, bearing 4 is embedded on the support of bearing 3, the support of bearing 3 is fixed on limiting bracket 1, limiting bracket 1 is by being welded to connect fixed support 2, fixed support 2 is fixed on heat exchanger end plate 9, limiting bracket 1, fixed support 2, the support of bearing 3, fixed axis 7, steady pin 8, bearing 4 all adopts food-grade 304 stainless steel to customize and forms, spiral band 5 adopts high molecular nanometer material to customize and forms.
During utility model works, limiting bracket 1 after fixing can ensure the die of the center of every root spiral band 5 and pipe type heat transfer pipe 6 at grade, such spiral band 5 two ends limiting bracket 1 spacing fixing under, can be smoothly in pipe type heat transfer pipe 6 inside, stable operation, limiting bracket 1, fixed support 2, the support of bearing 3, fixed axis 7, steady pin 8, bearing 4 all adopts food-grade 304 stainless steel to customize, spiral band 5 adopts high molecular nanometer material to customize and forms, the use of spiral band 5 pairs of pipe type heat transfer pipes 6 of high molecular nanometer material customization is without any negative effect, it can strengthen the heat transfer effect of tubular type heat exchanger tube 6, improve heat exchange efficiency, reduce energy waste, reach the object of energy-saving and emission-reduction consumption reduction, the incrustation scale of heat exchanger tube inwall can be removed momently, heat exchanger tube is made to be in the optimum condition of heat exchange all the time, spiral vinculum appts moves at heat exchange pipeline internal rotating, incrustation scale cannot be attached on tube wall, due to the flowing of water, current are through spiral band, current core space can be split into two halves by it, thus deflection water (flow) direction, the current making flow velocity higher fully mix with near-wall current, strengthen heat transfer effect, improve heat exchange efficiency about 30%, because this device is arranged on pipe heat exchanger inside, spiral band 5 two ends are fixed by fixed axis 7 respectively, fixed axis 7 is connected with bearing 4, bearing 4 is arranged on the support of bearing 3, and the support of bearing 3 weld or through fastened by screw on limiting bracket 1, limiting bracket 1 is welded on the end plate 9 of pipe heat exchanger through fixed support 2 again, such connected mode guarantees that spiral band 5 device runs freely in heat exchanger tube, the resistance of water in heat exchanger tube is reduced greatly, flow loss is also reduced to minimum, spiral band 5 in heat exchanger tube due to the flowing of water, the spiral band 5 connected through bearing 4 can rotate freely in heat exchanger tube, the dirt of tube wall can be removed by the spiral band 5 in rotation, all remove for making the dirt of pipe heat exchanger inside, the length of spiral band 5 is identical with the length of pipe heat exchanger, pipe heat exchanger operationally, fluid in pipe heat exchanger heat-transfer pipe is along the parallel flow forward of pipeline originally, the current of middle part cannot with tube wall contact heat-exchanging, heat exchange efficiency is caused to decline, due to the guide effect of spiral band, current are through spiral band, current core space can be split into two halves by it, thus deflection water (flow) direction, the current making flow velocity higher fully mix with near-wall current, strengthen heat transfer effect, improve heat exchange efficiency about 30%, reach energy-conservation object.
The foregoing is only the utility model preferred embodiment; not thereby embodiment of the present utility model and protection domain is limited; to those skilled in the art; the equivalent replacement that all utilization the utility model descriptions and diagramatic content are made and the scheme that apparent change obtains should be recognized, all should be included in protection domain of the present utility model.

Claims (6)

1. pipe type heat transfer energy saver, comprise limiting bracket (1), fixed support (2), the support of bearing (3), bearing (4), spiral band (5), fixed axis (7) and steady pin (8), it is characterized in that, pipe type heat transfer pipe inside is provided with spiral band (5), spiral band (5) is connected and fixed axle (7), fixed axis (7) is provided with bearing (4), bearing (4) is embedded on the support of bearing (3), the support of bearing (3) is fixed on limiting bracket (1), limiting bracket (1) is connected and fixed support (2), fixed support (2) is fixed on heat exchanger end plate (9).
2. pipe type heat transfer energy saver according to claim 1, is characterized in that, spiral band (5) is connected and fixed axle (7) by steady pin (8).
3. pipe type heat transfer energy saver according to claim 1, is characterized in that, steady pin (8) adopts riveting method to connect spiral band (5) and fixed axis (7).
4. pipe type heat transfer energy saver according to claim 1, is characterized in that, limiting bracket (1) is by being welded to connect fixed support (2).
5. pipe type heat transfer energy saver according to claim 1, it is characterized in that, limiting bracket (1), fixed support (2), the support of bearing (3), bearing (4), steady pin (8), fixed axis (7) all adopt food-grade 304 stainless steel to customize and form.
6. pipe type heat transfer energy saver according to claim 1, is characterized in that, spiral band (5) adopts the customization of high molecular nanometer material to form.
CN201520751406.3U 2015-09-26 2015-09-26 Tubular heat exchange energy conservation device Expired - Fee Related CN205049023U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520751406.3U CN205049023U (en) 2015-09-26 2015-09-26 Tubular heat exchange energy conservation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201520751406.3U CN205049023U (en) 2015-09-26 2015-09-26 Tubular heat exchange energy conservation device

Publications (1)

Publication Number Publication Date
CN205049023U true CN205049023U (en) 2016-02-24

Family

ID=55342595

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201520751406.3U Expired - Fee Related CN205049023U (en) 2015-09-26 2015-09-26 Tubular heat exchange energy conservation device

Country Status (1)

Country Link
CN (1) CN205049023U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106643270A (en) * 2016-12-01 2017-05-10 重庆渝青机械配件制造有限公司 Device with a plurality of cyclone spiral bands
CN107606975A (en) * 2017-10-18 2018-01-19 张少杰 A kind of pipe heat exchanger
CN109387090A (en) * 2018-10-26 2019-02-26 唐山钢铁集团有限责任公司 A kind of spiral condensing heat exchanger and heat-exchange method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106643270A (en) * 2016-12-01 2017-05-10 重庆渝青机械配件制造有限公司 Device with a plurality of cyclone spiral bands
CN107606975A (en) * 2017-10-18 2018-01-19 张少杰 A kind of pipe heat exchanger
CN109387090A (en) * 2018-10-26 2019-02-26 唐山钢铁集团有限责任公司 A kind of spiral condensing heat exchanger and heat-exchange method

Similar Documents

Publication Publication Date Title
CN205049023U (en) Tubular heat exchange energy conservation device
WO2012037745A1 (en) Self-cleaning enhanced heat transfer device used for heat exchange pipe and manufacturing method thereof
WO2016192130A1 (en) Sleeved pipe heat exchanger suitable for sewage having high solid content
CN203848750U (en) Back flushing circulating device of circulating water cooler
CN202109801U (en) Reinforced heat exchanging and automatic descaling apparatus for a heat exchanger pipeline
CN201697533U (en) Shell-and-tube condenser
CN103148719B (en) Heat exchanger
CN205580290U (en) Hydrogen -cooled ware online cleaning device
CN203550696U (en) Plate heat exchanger
CN101832731B (en) Tube type heat exchanger on-line antiscale and reinforcing heat exchange device
CN207300003U (en) A kind of pipe heat exchanger
CN103575128B (en) A kind of heat-exchanger rig fast
CN204594316U (en) A kind of on line cleaning device of forced-circulation evaporator
CN205748091U (en) Novel single tube circulating sleeve-type heat exchanger
CN207335528U (en) A kind of plate heat exchanger removes fouling device online
CN109696077A (en) A kind of the low thermal resistance automatically cleaning heat exchanger tube and condenser of enhanced heat exchange
CN204313673U (en) Spiral screw thread winding type heat exchanger
CN107129058A (en) Waste water industry TPL preheats antiscaling process
CN204177243U (en) The dry wet associating cooling tower of a kind of water-saving enclosed industrial circulating water
CN209445850U (en) A kind of silicon carbide tubular heat exchanger of high heat exchange efficiency
CN207922911U (en) A kind of exposure air box heat exchanger
CN2884109Y (en) High efficiency heat-exchanger of steam condenser, and said condenser
CN207662258U (en) A kind of the low thermal resistance automatically cleaning heat exchanger tube and condenser of enhanced heat exchange
CN208042871U (en) A kind of efficient primary cooler of automatically cleaning
CN101101187A (en) Internally spiral heat-exchanging tube

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20170706

Address after: 214000 Jiangsu city of Wuxi province new Wu Qutian road 8-708

Patentee after: Jiangsu high energy saving Technology Co., Ltd.

Address before: The 234105 Rail Town of Anhui province Suzhou City Yongqiao District HU 3 City Road District No. 124

Co-patentee before: Huang Zhongjun

Patentee before: Zhao Yancheng

CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20160224

Termination date: 20170926