CN100419366C - High efficiency plate pipe reverse running type square box heat exchanger - Google Patents
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- CN100419366C CN100419366C CNB2005100430000A CN200510043000A CN100419366C CN 100419366 C CN100419366 C CN 100419366C CN B2005100430000 A CNB2005100430000 A CN B2005100430000A CN 200510043000 A CN200510043000 A CN 200510043000A CN 100419366 C CN100419366 C CN 100419366C
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Abstract
The invention relates to a kind of high-effect tube-in-sheet back square-chest heat exchanger. Current sheet heat exchanger depends on the mutual extrusion among sheets to be sealed. And it uses the reverse groove pressed by sheets as the flow passage. The space of the flow passage is narrow and it is often jammed by the tiny filth. So the equipment often needs to clear. It influences the heat exchanging effect and the normal using of the equipment and brings inconvenience for users. The single pass and the single flow passage make thermal efficiency low, energy sources loss high and operating charge expensive. The invention adopts the tube-in-sheet back square-chest heat exchanger. It forms multi-pass, multi-passage and multi-baffle path by the baffle board, the tube-in-sheet baffle board and the guide board in the chest. It not only has the tight structure and the small capacity, but also has high heat exchange coefficient, small heat exchange area and low cost.
Description
One, technical field:
The present invention relates to heat exchanger, is a kind of high efficiency plate pipe reverse running type square box heat exchanger specifically.
Two, technical background:
In the prior art, existing plate type heat exchanger finds that by long term studies and user's actual behaviour in service mainly there is following shortcoming in existing plate type heat exchanger:
1, runner gap Xiao Yi stops up, and flow velocity diminishes, instability of flow, and the dilatation diffusion does not have and is pressed.
Because plate type heat exchanger is to rely on plate and plate mutual extrusion to seal, utilize the groove of plate punching press as runner, the runner gap is little, often stop up runner because of tiny dirt, therefore need often equipment to be cleared up, influence the heat exchange effect and normal use of equipment, caused inconvenience to the user.
2, one-stroke, single channel, equipment thermal efficiency is low, wastes energy the operating cost height.
Plate type heat exchanger primary fluid and secondary heating agent are one-stroke, and haul distance is 3/4 of a plate height.Because plate type heat exchanger primary fluid and secondary heating agent are one-stroke, and primary fluid and secondary heating agent stroke weak point.Primary fluid is also utilizing the end that just arrive runner fully, and the also not utilizations once more of these heating agents that do not utilize fully, and the heating agent utilization rate only is about 50%, has wasted a large amount of available energys, has increased expense, to around cause thermal pollution; The secondary heating agent must heat also not absorbing fully reaches institute must temperature the time, has arrived the end of runner, and electric energy has been wasted in the heating that must repeatedly circulate repeatedly, has increased the operating cost of equipment.General plate-type heat-exchange heat transfer coefficient (K value), vapour-water heat exchange heat transfer coefficient (K value) is 3000-5000W/ (m
2.k); Water-water heat exchange heat transfer coefficient (K value) is 800-1200W/ (m
2.k).
3, plate is perishable, easily perforation.Must change plate, sealing strip, invest once more, user's investment cost is increased once more, and the equipment that influenced normally use.
4, maintenance of equipment expense height.Because sealing is to rely on the rubber strip crush seal between the plate type heat exchanger plate, rubber strip crimp is added and is heated, and must all must open by every sheet during overhaul of the equipments, and in a single day plate is opened major part and just can not be used, and must change.The price that the rubber strip list is bought is all very high, has brought rubber strip and the artificial very big expense bought to the user.
5, material: existing plate type heat exchanger plate all adopts stainless steel material, because of containing the CL ion in China's most of province water, and the CL ion contacts meeting generation chemical reaction with stainless steel, plate is formed corrosion, and general plate type heat exchanger plate is after using 2 years, and some plates are just very thin or bored a hole because of CL ion etching plate wall, must change plate, invest once more, user's investment cost is increased once more, and the equipment that influenced normally uses.
6, lack service life, plate type heat exchanger limits because of its structure and material, and service life is generally at 2-3.
7, simple in structure, no outer cover packaging, and also profile is not attractive in appearance, practical.
Three, summary of the invention:
The purpose of this invention is to provide a kind of high efficiency plate pipe reverse running type square box heat exchanger that can raise the efficiency, reduce cost and dwindle space.
For achieving the above object, the technical solution used in the present invention:
High efficiency plate pipe reverse running type square box heat exchanger comprises heat exchanger, heating agent outlet 2, heating agent import 9, high-temperature steam import 1, condensate water outlet 10, its respectively with heat exchanger on heat exchanger tube and the import and export of housing is connected the formation heat-exchange device; Its special character is: described plate pipe backhaul heat exchanger is a square chest type structure, and it is made of deflector 5, square tube sheet 6, square flange end socket 7 in deflection plate 11, a plurality of tube sheet deflection plate 8, a plurality of casing in square cylindrical shell 3, many heat exchanger tubes 4, a plurality of casing; Described many heat exchanger tubes 4 are arranged on the square tube sheet 6; Deflection plate 11 is horizontally set in the square cylindrical shell 3 in a plurality of casings in the described square chest type heat exchanger, constitutes a plurality of cavitys, shifts to install successively about the import and export of each cavity; Deflector 5 is vertically set in the square cylindrical shell 3 in a plurality of casings in the described square chest type heat exchanger, shifts to install successively before and after the import and export of a plurality of cavitys of its formation; The square tube sheet 6 of described square chest type heat exchanger, square flange end socket 7 constitute outer chamber, and a plurality of tube sheet deflection plates 8 are set in it, constitute the backhaul passage.
Deflection plate 11 constitutes a plurality of cavitys up and down in a plurality of casings in the above-mentioned square chest type heat exchanger, and the quantity of the many heat exchanger tubes 4 in each cavity is successively decreased from top to bottom successively.
Above-mentioned square tube sheet 6, and square flange end socket 7 between be the flange type of attachment.
Above-mentioned heat exchanger tube 4 adopts nonferrous metal tube.
The present invention is with respect to prior art, and its advantage is as follows:
Tube sheet backhaul heat exchanger shell adopts low alloy steel plate to make, and heat-exchanging tube bundle is that tubule is formed, and it can be copper tube, nickel alloy or Nitinol pipe.The general advantage of this heat exchanger is pressed droop loss little as the bearing capacity height, regional efficiency of heating surface height, and heat resistance is good, the manufacturing process maturation, capacity big (be other heat exchangers to escort services), cost is lower, outside the performances such as maintenance management is easy, long service life also has following important feature:
1, tube sheet backhaul heat exchanger structure adopts the square chest type profile, and compact conformation is small, saves land area and building height.It is in light weight, at the bottom of the cost, increases operation rate greatly, saves construction investment, is convenient to design arrangement, and operation is simultaneously made and done conveniently.
2, the spacing of the gap ratio plate type heat exchanger of the steam passage of tube sheet backhaul heat exchanger and water channel is big several times, is not easy to stop up.The heat-exchanging tube bundle subdivision arranges that the size and the weight of each unit heat-exchanging tube bundle are less, is convenient to safeguard and clean.
3, good sealing effect keeps more than the 5-10, and the housing of tube sheet backhaul heat exchanger connects the employing welding, and heat-exchanging tube bundle and tube sheet adopt expanded joint, and be solid and reliable.Each unit of heat-exchanging tube bundle independently is provided with,
4, craft science, easy access, process pipe is convenient to install, and each unit of heat-exchanging tube bundle independently is provided with, and only need open heat exchanger front and back end socket during maintenance, heat-exchanging tube bundle is inner to come into plain view, simple and convenient, pipe has been broken only to need to extract out and has been changed never fouling, end socket and tube sheet sealing plate can use repeatedly, generally mustn't change.
5, heat transfer coefficient height is saved heat exchange area, general tube sheet backhaul heat exchanger heat transfer coefficient (K value), and vapour-water heat exchange heat transfer coefficient (K value) is 10400-10700W/ (m
2.k) about; Water-water heat exchange heat transfer coefficient (K value) is 2800-3100W/ (m
2.k), vapour-water heat exchange is bigger about 1.5 times than plate type heat exchanger, and heat exchange area can reduce 40-60%; Water-water heat exchange heat transfer coefficient is than the high 30-40% of general light pipe heat exchanger.
6, new high-efficiency, zone heating, heat utilization height.The condensing water temperature that plate pipe backhaul heat exchanger vapour-water heat exchange is discharged is low both not to have had leakage losses generally below 70 ℃, did not need to install steam trap yet.The heat exchange zone is not in the same space: multiple-pass, multithread road, many bafflings.The zone heating divides five (six) districts from top to bottom: (low temperature low district heating) low temperature high district heating, the low district heating of middle temperature, middle Wen Gaoqu heating, high temperature low district heating, high temperature high district heating.The subregion heating, the runner lengthening, and all be the adverse current heating, its heat exchange is abundant.
7, the condensate water pressure of plate pipe backhaul heat exchanger vapour-water heat exchange discharge is 80% of steam pressure, can utilize the overbottom pressure of self to be back to the boiler room.Saved the equipment and the station investment of condensate return system, it is all greatly convenient to design simultaneously and manage.
8, hydraulic characteristic(s) is good, and heating agent is little with the flow resistance that is heated water, flow speed stability.
9, long service life, be 15-20 service life.
Four, description of drawings:
Fig. 1 is the assembly structure schematic diagram of existing plate-type heat-exchange;
Fig. 2 is the cross-sectional view of plate pipe backhaul heat exchanger of the present invention;
Fig. 3 is the horizontal profile structure schematic diagram of plate pipe backhaul heat exchanger of the present invention;
Fig. 4 is the perspective view of the casing of plate pipe backhaul heat exchanger of the present invention;
The number in the figure explanation:
1-high-temperature steam import 2-heating agent outlet 3-square cylindrical shell
Deflector 6-square tube sheet in the 4-heat exchanger tube 5-casing
The import of 7-square flange end socket 8-tube sheet deflection plate 9-heating agent
Deflection plate in the 10-condensate water outlet 11-casing
Five, the specific embodiment:
Referring to Fig. 1, existing plate type heat exchanger, because plate type heat exchanger is to rely on plate and plate mutual extrusion to seal, utilize the groove of plate punching press as runner, the runner gap is little, often stop up runner because of tiny dirt, therefore need often equipment to be cleared up, influence the heat exchange effect and normal use of equipment, caused inconvenience to the user.And it is one-stroke, single channel, and equipment thermal efficiency is low, wastes energy the operating cost height.
Referring to Fig. 2, Fig. 3, Fig. 4, plate pipe backhaul heat exchanger of the present invention is a square chest type structure, it is made of deflector 5, square tube sheet 6, square flange end socket 7 in deflection plate 11, a plurality of tube sheet deflection plate 8, a plurality of casing in square cylindrical shell 3, many heat exchanger tubes 4, a plurality of casing; Described many heat exchanger tubes 4 are arranged on the square tube sheet 6;
Deflection plate 11 is horizontally set in the square cylindrical shell 3 in a plurality of casings in the square chest type heat exchanger, constitutes a plurality of cavitys, shifts to install successively about the import and export of each cavity;
Square tube sheet 6, square flange end socket 7 at the square chest type heat exchanger constitute outer chamber, and a plurality of tube sheet deflection plates 8 are set in it, constitute the backhaul passage.
Thereby the heat exchange zone does not form multiple-pass, multithread road, many bafflings in the same space.The zone heating divides five (six) districts from top to bottom: (thermal treatment zone, the low district of low temperature) low temperature Gao Qu thermal treatment zone, the thermal treatment zone, the low district of middle temperature, the middle Wen Gaoqu thermal treatment zone, the thermal treatment zone, the low district of high temperature, the high temperature Gao Qu thermal treatment zone.It adopts the subregion heating, the runner lengthening, and all be the adverse current heating, its heat exchange is abundant.
In a plurality of cavitys, in order to reduce pressure drop, guarantee flow velocity about deflection plate 11 constitutes in a plurality of casings in the square chest type heat exchanger, the quantity of the many heat exchanger tubes 4 in each cavity is successively decreased from top to bottom successively.
Tube sheet is designed to many backhauls, and the zone heating divides from top to bottom: low-temperature space heating, the low district heating of middle temperature, middle Wen Gaoqu heating, high temperature low district heating, high temperature high district heating.With being threaded, square cylinder and two tube sheets are welding for the ease of maintenance flange and tube sheet, and tube-to-tube sheet connection is an expanded joint, in order to be that its stroke extends, heat fully, have welded many deflection plates up and down in the bobbin carriage, many deflectors have been welded in front and back.Pipe and the cylindrical shell/flange imported and exported are to be welded to connect.
Referring to Fig. 2, Fig. 3, Fig. 4, the operation principle of plate pipe backhaul heat exchanger is: high-temperature steam or high-temperature water flow into left type tube sheet 6 by high-temperature steam import 1, high-temperature steam or high-temperature water enter heat exchanger tube 4 by the tube sheet water conservancy diversion, high-temperature steams or high-temperature water following current enter in the square flange end socket 7 in the heat exchanger tube 4, and the water conservancy diversion by right-hand type tube sheet and the baffling of end socket be from the high inflow high temperature base area of distinguishing of high temperature again, and the pipe number of tube sheet and the flow flow velocity that successively decreases is constant.Arrive in the left type flange end socket by heat exchanger tube 4 adverse currents then, by the water conservancy diversion of left tube sheet and baffling Wen Gaoqu from the high temperature base area flows into of end socket, the pipe number and the flow of tube sheet successively decrease again, arrive in the square flange end socket 7 by heat exchanger tube 4 following currents then, the baffling of the water conservancy diversion by right tube sheet and end socket warm base area in the Wen Gaoqu inflow therefrom once more, flow successively decreases once more, arrive in the left end socket by the heat exchanger tube adverse current, flow into temperature base area, the end by the water conservancy diversion of left tube sheet and the therefrom warm base area of baffling of end socket, in left end socket, permanent set water is discharged by the heat exchanger tube following current.
Be to be heated heating agent in the square cylindrical shell 3, be heated heating agent and enter housing by heating agent import 9, then by front and back water conservancy diversion and left and right sides baffling, flow velocity slows down, and make shape journey lengthening, by the heating of heating tube zone, heating fully, mainly show: fifth line journey primary fluid heats the secondary heating agent of first stroke, fourth line journey primary fluid heats the secondary heating agent of second stroke, the third trip primary fluid heats three heating agents of first stroke, the secondary heating agent of second stroke primary fluid heating fourth line journey, the secondary heating agent of first stroke primary fluid heating fifth line journey.Heating agent outlet outflow from the top is used for heat supply then, and high-temperature steam or water enter from the height district then and successively decreases to low district gradually by tube sheet and deflector, flow out from heating agent outlet 2 then; Plate pipe backhaul heat exchanger is by the heating agent in the heat exchanger tube heating shell with high-temperature steam or water.
The present invention has adopted the tubule composition, and nonferrous metal tube is a runner., instability of flow little at the plate type heat exchanger flow velocity, the return-stroke type tube sheet that has adopted heat exchanger tube quantity, flow to successively decrease has guaranteed that flow velocity is constant.In order to reduce maintenance cost, the present invention has adopted fixed tube sheet, flange to connect, easy to assemble, maintenance, and pipe has been broken only to need to extract out and has been changed.In order to improve equipment thermal efficiency, effective use of energy sources, the present invention has adopted water bag vapour and has adopted multiple-pass, multithread road, many bafflings, formed the local adverse current heating of each heat transfer space, heat exchange is abundant, and interior pipe resistance is little, is pressed at the bottom of the temperature, droop loss is few by pressing, and safety and stability is compared in work.The present invention has adopted square chest type structure, and compact conformation is attractive in appearance, and is small, and volume is big, is three times of general heat exchanger, saves land area and building height, saves construction investment, is convenient to design arrangement, and operation is convenient simultaneously.The present invention adopts low alloy steel plate and non-ferrous alloy to make and has effectively prevented corrosion.The bearing capacity height, by being pressed droop loss little, regional efficiency of heating surface height, heat resistance is good, and manufacturing process is good, and cost is lower, long service life, performance such as maintenance management is easy has effectively prevented some disadvantages of other heat exchangers.
High efficiency plate pipe reverse running type square box heat exchanger of the present invention, it is applicable to that generally the steam of the various parameters that each department municipal heating systems, district heating or individual consumer boiler room are supplied and high-temperature-hot-water use as the heat exchange station of heating agent, also can satisfy various industrial specific uses.Can be used for various heating in common building, skyscraper and the high-rise building, air-conditioning circulation water for heating system and domestic hot-water's circulation.
The heating agent that the high-temperature steam import enters can be high-temperature water, waits primary fluid.
Claims (4)
1. high efficiency plate pipe reverse running type square box heat exchanger comprises heating agent outlet (2), heating agent import (9), high-temperature steam import (1), condensate water outlet (10); Heating agent outlet (2), heating agent import (9), high-temperature steam import (1), condensate water outlet (10) respectively with heat exchanger on heat exchanger tube and the import and export of housing is connected the formation heat-exchange device; It is characterized in that: described high efficiency plate pipe reverse running type square box heat exchanger is a square chest type structure, and it is made of deflector (5), square tube sheet (6), square flange end socket (7) in deflection plate (11), a plurality of tube sheet deflection plate (8), a plurality of casing in square cylindrical shell (3), many heat exchanger tubes (4), a plurality of casing; Described many heat exchanger tubes (4) are arranged on the square tube sheet (6); Deflection plate (11) is horizontally set in the square cylindrical shell (3) in a plurality of casings in the described square chest type heat exchanger, constitutes a plurality of cavitys, shifts to install successively about the import and export of each cavity; Deflector (5) is vertically set in the square cylindrical shell (3) in a plurality of casings in the described square chest type heat exchanger, shifts to install successively before and after the import and export of a plurality of cavitys of its formation; The square tube sheet (6) of described square chest type heat exchanger, square flange end socket (7) constitute outer chamber, and a plurality of tube sheet deflection plates (8) are set in it, constitute the backhaul passage.
2. high efficiency plate pipe reverse running type square box heat exchanger according to claim 1, it is characterized in that: the interior deflection plate (11) of a plurality of casings in the described square chest type heat exchanger constitutes a plurality of cavitys up and down, and the quantity of the heat exchanger tube (4) about each that deflection plate (11) constitutes in a plurality of casings in the cavity is successively decreased from top to bottom successively.
3. high efficiency plate pipe reverse running type square box heat exchanger according to claim 1 and 2 is characterized in that: described square tube sheet (6), and square flange end socket (7) between for the flange type of attachment.
4. high efficiency plate pipe reverse running type square box heat exchanger according to claim 3 is characterized in that: described heat exchanger tube (4) adopts nonferrous metal tube.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100430000A CN100419366C (en) | 2005-07-27 | 2005-07-27 | High efficiency plate pipe reverse running type square box heat exchanger |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100430000A CN100419366C (en) | 2005-07-27 | 2005-07-27 | High efficiency plate pipe reverse running type square box heat exchanger |
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| CN1904537A CN1904537A (en) | 2007-01-31 |
| CN100419366C true CN100419366C (en) | 2008-09-17 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101929808A (en) * | 2010-05-30 | 2010-12-29 | 大连海新工程技术有限公司 | Box-type multi-tube pass heat exchanger |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105758230A (en) * | 2014-12-17 | 2016-07-13 | 中国石油天然气股份有限公司 | Heat exchanger for crude oil produced liquid |
| CN113893795B (en) * | 2021-10-14 | 2023-04-25 | 中北大学 | Continuous aging device and method in pseudo-boehmite preparation process |
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| CN2101208U (en) * | 1991-09-28 | 1992-04-08 | 上海市化工装备研究所 | High-efficiency heat exchanger |
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| JPH07305984A (en) * | 1994-05-10 | 1995-11-21 | Hitachi Ltd | Heat exchanger |
| CN2301695Y (en) * | 1997-01-31 | 1998-12-23 | 刘振印 | Minor spiral guide multiple pass fast heat exchanger |
| CN2335112Y (en) * | 1998-08-06 | 1999-08-25 | 华南理工大学 | Low flow-resistant shell structure pipe-shell type heat-exchanger |
| CN2384188Y (en) * | 1999-08-12 | 2000-06-21 | 江苏双良锅炉有限公司 | Reducing flow area heat exchanger |
| CN2618126Y (en) * | 2003-01-22 | 2004-05-26 | 卢秉威 | Square modular heat exchanger |
| CN2861933Y (en) * | 2005-07-27 | 2007-01-24 | 西安华广电站锅炉有限公司 | Efficient plate and tube back type square box heat exchanger |
-
2005
- 2005-07-27 CN CNB2005100430000A patent/CN100419366C/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2101208U (en) * | 1991-09-28 | 1992-04-08 | 上海市化工装备研究所 | High-efficiency heat exchanger |
| CN2127996Y (en) * | 1992-07-16 | 1993-03-10 | 谷林 | Corrosion resistant columm pipe type heat exchanger |
| JPH07305984A (en) * | 1994-05-10 | 1995-11-21 | Hitachi Ltd | Heat exchanger |
| CN2301695Y (en) * | 1997-01-31 | 1998-12-23 | 刘振印 | Minor spiral guide multiple pass fast heat exchanger |
| CN2335112Y (en) * | 1998-08-06 | 1999-08-25 | 华南理工大学 | Low flow-resistant shell structure pipe-shell type heat-exchanger |
| CN2384188Y (en) * | 1999-08-12 | 2000-06-21 | 江苏双良锅炉有限公司 | Reducing flow area heat exchanger |
| CN2618126Y (en) * | 2003-01-22 | 2004-05-26 | 卢秉威 | Square modular heat exchanger |
| CN2861933Y (en) * | 2005-07-27 | 2007-01-24 | 西安华广电站锅炉有限公司 | Efficient plate and tube back type square box heat exchanger |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101929808A (en) * | 2010-05-30 | 2010-12-29 | 大连海新工程技术有限公司 | Box-type multi-tube pass heat exchanger |
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| CN1904537A (en) | 2007-01-31 |
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