CN103512401A - Spiral-plate heat exchanger with protection function - Google Patents
Spiral-plate heat exchanger with protection function Download PDFInfo
- Publication number
- CN103512401A CN103512401A CN201310493763.XA CN201310493763A CN103512401A CN 103512401 A CN103512401 A CN 103512401A CN 201310493763 A CN201310493763 A CN 201310493763A CN 103512401 A CN103512401 A CN 103512401A
- Authority
- CN
- China
- Prior art keywords
- heat
- heat exchanger
- spiral
- flow plate
- plate
- 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.)
- Granted
Links
Images
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention relates to a spiral-plate heat exchanger with the protection function. The spiral-plate heat exchanger structurally comprises a heat flow plate and a cold flow plate. The heat flow plate is connected with the cold flow plate in a spiral and winding mode. A pressure releasing hole is formed in the heat flow plate, a pressure releasing device is arranged inside the pressure releasing hole, and the pressure releasing device is composed of two valve elements, a valve cylinder and a spring, wherein the valve cylinder is installed inside the pressure releasing hole, and the two valve elements are oppositely placed at the two ends inside the valve cylinder and are connected through the spring. A filtering device is arranged in an inlet of the heat flow plate. According to the spiral-plate heat exchanger, impurities in materials conveyed into the heat flow plate can be filtered out, and a channel is prevented from being blocked. The automatic pressure releasing device is installed on the heat flow plate, and therefore the structure of the heat flow plate is prevented from being damaged by too large pressure. Due to the fact that a plurality of circulation devices are arranged, the accuracy of heat flow transmission is guaranteed, the cyclic utilization of the cold flow materials is achieved, and cost is reduced. Energy sources can be recycled through the spiral-plate heat exchanger, the waste of the energy sources is reduced, and practicability is improved.
Description
Technical field
The present invention relates to a kind of heat transmission equipment, particularly a kind of spiral heat exchanger with defencive function.
Technical background
Plate type heat exchanger is a kind of new type high efficient heat exchanger being formed by a series of sheet metal closed assemblies with certain bellows-shaped.Between various plates, form thin rectangular shape passage, by half sheet, carry out exchange heat.Plate type heat exchanger is the ideal equipment that liquid-liquid, liquid-vapour carry out heat exchange.The features such as it has that heat exchange efficiency is high, heat loss is little, advantages of compact and light structure, floor space are little, easy to clean is installed, be widely used, long service life.Under uniform pressure damaed cordition, doubly, floor space is pipe heat exchanger to the high 3-5 of its ratio of heat transfer coefficient pipe heat exchanger 1/3rd, and heat recovery rate can be up to more than 90%.Spiral heat exchanger is a kind of high-performance heat exchanger equipment, and applicable vapour-vapour, vapour-liquid, liquid-liquid, conduct heat to liquid.It is applicable to the industries such as chemistry, oil, solvent, medicine, food, light industry, weaving, metallurgy, steel rolling, coking.Compared to some, other plate type heat exchanger has advantages of that contact area is large, heat transfer rate is fast, efficiency is high to spiral heat exchanger.
Chinese invention patent discloses a kind of helical form plate type heat exchanger No. CN102809313A, its structure includes and rolls rear spiral heat exchanger main body, between adjacent spiral coil, be formed with spiral heat exchanger channels, in the outer ring of spiral coil, adjacent is provided with flue side seal board, in heat exchanger main body, be provided with intake tunnel and exhalant canal, between intake tunnel and exhalant canal, by flow distribution plate, be spaced from each other.There is not pressure control and anti-block apparatus in this structure, has at work this potential safety hazard, can not meet modernization industry Production requirement.
Summary of the invention
The technical issues that need to address of the present invention are prevent from being delivered into the impurity blocking channel of material in heat flux plates and prevent the excessive structural deterioration that causes heat exchanger of pressure in heat flux plates; A kind of spiral heat exchanger with defencive function is provided.
For solving above-mentioned technical problem, structure of the present invention comprises heat flux plates, cold flow plate, heat flux plates is connected with cold flow plate spiral winding, in described heat flux plates, also have relief hole, pressure relief device is housed in relief hole, described pressure relief device is comprised of two spools, valve cylinder and springs, valve cylinder is contained in relief hole, two spools are relatively arranged at valve cylinder Nei two ends, and two spools connect by spring, and filter is also equipped with in the porch of heat flux plates.
Further again: described cold flow Ban two ends are connected with the first circulation pipe, and the first circulation pipe is provided with condenser, are also provided with heat power collection generator between the outlet of cold flow plate and condenser.
Further again: described heat power collection generator forms by being connected in the heat collector of the first circulation pipe, the heat exchanger being connected with heat collector, heat generator and circulating pump; Heat exchanger, heat generator and circulating pump are connected successively by the second circulation pipe.
Further again: the two ends of described heat flux plates are also connected with return duct, and return duct is provided with gauge tap, gauge tap is connected with storage tank with thermometer respectively.
Further again: described filter is liquid filter or gas dust remover.
Adopt after said structure, the present invention can filter out the impurity that is delivered into material in heat flux plates, prevents the generation that passage stops up; Automatic decompression device is equipped with in the present invention in heat flux plates, prevents the excessive generation that causes self structure to destroy of heat flux plates internal pressure; The present invention is provided with the accuracy that a plurality of EGRs have not only guaranteed that hot-fluid transmits, and has realized recycling of cold flow material, has reduced cost; The present invention has also realized the regeneration of the energy, and unnecessary heat collection is got up to generate electricity, and has reduced the waste of the energy, has increased the design's practicality.
Accompanying drawing explanation
Below in conjunction with the drawings and specific embodiments, the present invention is further detailed explanation.
Fig. 1 is structural representation of the present invention.
Fig. 2 is 1 and 2 annexation figure in Fig. 1.
Fig. 3 is the structural representation of A in Fig. 1.
In figure: 1 is cold flow plate, 2 is heat flux plates, and 3 is the first circulation pipe, 4 is return duct, and 5 is heat generator, and 6 is the second circulation pipe, 7 is circulating pump, and 8 is condenser, and 9 is heat exchanger, 10 is heat collector, and 11 is thermometer, and 12 is storage tank, 13 is gauge tap, and 14 is filter, and 15 is spring, 16 is valve cylinder, and 17 is spool, and 18 is relief hole
The specific embodiment
A kind of spiral heat exchanger with defencive function as shown in Figure 1, Figure 2 and Figure 3; comprise heat flux plates 2, cold flow plate 1; heat flux plates 2 is connected with cold flow plate 1 spiral winding; it is characterized in that: in described heat flux plates 2, also have relief hole 18; in relief hole 18, pressure relief device is housed; described pressure relief device is comprised of two spools 17, valve cylinder 16 and spring 15; valve cylinder 16 is contained in relief hole 18; two spools 17 are relatively positioned over valve cylinder 16Nei two ends, and two spools 17 connect by spring 15.During work, to heat flux plates 2 and cold flow plate 1 transportation of substances, conduct heat simultaneously, because the temperature of heat flux plates 2 interior materials is higher, pressure in it is also just higher, when its pressure surpasses the critical value that self structure bears, will produce blast, and machine and other people are caused to unnecessary injury.This structure by setting up 2 relief holes 18 in heat flux plates 2; the pressure relief device being comprised of two spools 17, valve cylinder 16 and spring 15 is housed in relief hole 18; when pressure is excessive; pressure can promote spring 15; gases at high pressure or liquid will be discharged from spool 17 and valve cylinder 16 space; reduce the pressure in heat flux plates 2, self structure is played a protective role.Heat flux plates 2 of the present invention and cold flow plate 1 adopted spiral winding to be connected to increase the contact area of hot and cold of heat exchanger, improved the operating efficiency of heat exchanger.
The two ends of cold flow plate 1 are as shown in Figure 1 connected with the first circulation pipe 3, the first circulation pipes 3 and are provided with condenser 8, between the outlet of cold flow plate 1 and condenser 8, are also provided with heat power collection generator.Described heat power collection generator forms by being connected in the heat collector 10 of the first circulation pipe 3, the heat exchanger 9 being connected with heat collector 10, heat generator 5 and circulating pump 7; Heat exchanger 9, heat generator 5 and circulating pump 7 are connected successively by the second circulation pipe 6.Medium in cold flow plate 1 has higher temperature after completing heat transfer, if just can not recycle to medium cooling, has greatly wasted resource.So the present invention is provided with condenser 8 on the first circulation pipe 3, this design is in order to recycle to medium cooling.If temperature wastes and can cause greatly energy waste in the medium in cold flow plate 1, so had additional heat power collection generator in the present invention between the outlet of cold flow plate 1 and condenser 8, by heat collector 10, gather the heat of medium in cold flow plate, these heats are passed to the medium of the second circulation pipe 6 by heat exchanger 9, the medium of the second circulation pipe 6 heat generator 5 of flowing through under the effect of circulating pump 7 generates electricity, finally flow back into again heat exchanger 9, complete the regeneration of the energy.
The two ends of heat flux plates 2 as shown in Figure 1 are also connected with return duct 4, and return duct 4 is provided with gauge tap 13, and gauge tap 13 is connected with storage tank 12 with thermometer 11 respectively.This design is in order to ensure needing the temperature of cooling material to meet the requirements, after temperature that thermometer 11 records material meets the demands, gauge tap 13 can be discharged into material in storage tank 12, when the temperature of material undesirable, material again flow in heat flux plates 2 by return duct 4 under the effect of gauge tap 13, carries out heat transfer again.
Filter 14 is also equipped with in the porch of heat flux plates 2 as shown in Figure 1, and described filter 14 is liquid filter or gas dust remover.This design is the impurity that is delivered into material in heat flux plates with removing, and prevents the generation that passage stops up; In the liquid that need to lower the temperature or gas, likely exist a large amount of impurity, when being deposited in a place, these impurity unifications are easy to form the obstruction of passage, not only reduced operating efficiency, and easily cause danger, so this design is very necessary, the material of not only having purified, but also played the effect that Accident prevention occurs.
In sum the present invention have simple in structure, be easy to the advantages such as manufacture, Environmental Safety, heat transfer rate be fast, there is the good market competitiveness.
Claims (5)
1. the spiral heat exchanger with defencive function, comprise heat flux plates (2), cold flow plate (1), heat flux plates (2) is connected with cold flow plate (1) spiral winding, it is characterized in that: in described heat flux plates (2), also have relief hole (18), relief hole is equipped with pressure relief device in (18), described pressure relief device is by two spools (17), valve cylinder (16) and spring (15) form, valve cylinder (16) is contained in relief hole (18), two spools (17) are relatively positioned over valve cylinder (16) Nei two ends, two spools (17) connect by spring (15), filter (14) is also equipped with in the porch of heat flux plates (2).
2. a kind of spiral heat exchanger with defencive function according to claim 1; it is characterized in that: the two ends of described cold flow plate (1) are connected with the first circulation pipe (3); the first circulation pipe (3) is provided with condenser (8), between the outlet of cold flow plate (1) and condenser (8), is also provided with heat power collection generator.
3. a kind of spiral heat exchanger with defencive function according to claim 2, is characterized in that: described heat power collection generator forms by being connected in the heat collector (10) of the first circulation pipe (3), the heat exchanger (9) being connected with heat collector (10), heat generator (5) and circulating pump (7); Heat exchanger (9), heat generator (5) and circulating pump (7) are connected successively by the second circulation pipe (6).
4. a kind of spiral heat exchanger with defencive function according to claim 1; it is characterized in that: the two ends of described heat flux plates (2) are also connected with return duct (4); return duct (4) is provided with gauge tap (13), and gauge tap (13) is connected with storage tank (12) with thermometer (11) respectively.
5. a kind of spiral heat exchanger with defencive function according to claim 1, is characterized in that: described filter (14) is liquid filter or gas dust remover.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310493763.XA CN103512401B (en) | 2013-10-20 | 2013-10-20 | Spiral-plate heat exchanger with protection function |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310493763.XA CN103512401B (en) | 2013-10-20 | 2013-10-20 | Spiral-plate heat exchanger with protection function |
Publications (2)
Publication Number | Publication Date |
---|---|
CN103512401A true CN103512401A (en) | 2014-01-15 |
CN103512401B CN103512401B (en) | 2015-03-25 |
Family
ID=49895522
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201310493763.XA Expired - Fee Related CN103512401B (en) | 2013-10-20 | 2013-10-20 | Spiral-plate heat exchanger with protection function |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103512401B (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110736370A (en) * | 2018-07-18 | 2020-01-31 | 兰州兰洛炼化高新装备股份有限公司 | Mixed flow passage spiral plate type heat exchanger |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1375051A (en) * | 1999-09-20 | 2002-10-16 | 阿尔法拉瓦尔有限公司 | A spiral heat exchanger |
US20020148600A1 (en) * | 2001-04-05 | 2002-10-17 | Bosch Daniel J. | Spiral fin/tube heat exchanger |
CN101118133A (en) * | 2007-09-06 | 2008-02-06 | 杨杰 | Novel slab type spiral heat exchanger |
CN102224367A (en) * | 2008-11-21 | 2011-10-19 | 达纳加拿大公司 | Thermal by-pass valve with pressure relief capability |
JP5247357B2 (en) * | 2008-10-30 | 2013-07-24 | 三機工業株式会社 | Spiral heat exchanger and engine performance test device |
CN203550697U (en) * | 2013-10-20 | 2014-04-16 | 丹阳市正大油脂有限公司 | Spiral plate heat exchanger with protection function |
-
2013
- 2013-10-20 CN CN201310493763.XA patent/CN103512401B/en not_active Expired - Fee Related
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1375051A (en) * | 1999-09-20 | 2002-10-16 | 阿尔法拉瓦尔有限公司 | A spiral heat exchanger |
US20020148600A1 (en) * | 2001-04-05 | 2002-10-17 | Bosch Daniel J. | Spiral fin/tube heat exchanger |
CN101118133A (en) * | 2007-09-06 | 2008-02-06 | 杨杰 | Novel slab type spiral heat exchanger |
JP5247357B2 (en) * | 2008-10-30 | 2013-07-24 | 三機工業株式会社 | Spiral heat exchanger and engine performance test device |
CN102224367A (en) * | 2008-11-21 | 2011-10-19 | 达纳加拿大公司 | Thermal by-pass valve with pressure relief capability |
CN203550697U (en) * | 2013-10-20 | 2014-04-16 | 丹阳市正大油脂有限公司 | Spiral plate heat exchanger with protection function |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110736370A (en) * | 2018-07-18 | 2020-01-31 | 兰州兰洛炼化高新装备股份有限公司 | Mixed flow passage spiral plate type heat exchanger |
Also Published As
Publication number | Publication date |
---|---|
CN103512401B (en) | 2015-03-25 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE102011000655B4 (en) | heat transport system | |
CN204303368U (en) | Fixed gas retracting device in a kind of radioactive liquid waste evaporation process | |
CN107328253A (en) | A kind of My heat recovery system of sewage | |
CN103063058A (en) | Novel horizontal cooler | |
CN201772776U (en) | High-efficiency heat exchanger provided with flue gas purification and filtration function | |
CN203550697U (en) | Spiral plate heat exchanger with protection function | |
CN103512401B (en) | Spiral-plate heat exchanger with protection function | |
CN102908855A (en) | Waste heat utilizing and waste oil wax recycling device for heat-setting machine | |
CN208474053U (en) | A kind of wind-driven generator group wheel box cooling heat radiation system | |
CN104405622A (en) | Novel air compression station system | |
CN102974165A (en) | Centrifugal oil purifier | |
CN103953961A (en) | High back pressure and heat pump combined heat supply system for air cooling unit | |
CN210251269U (en) | Efficient heat-conducting oil online lightness removing device | |
CN201297257Y (en) | Efficient heat recovery system of air compressor | |
CN207391389U (en) | A kind of liquor production is with being quickly cooled down tank | |
CN204026650U (en) | The single-row high-pressure heater system of 1000MW level double reheat unit | |
CN202777891U (en) | Filtering and cooling system for recycling waste gas | |
CN203098292U (en) | Waste heat recycling system of air compressor | |
CN205747616U (en) | A kind of UTILIZATION OF VESIDUAL HEAT IN coolant reclaiming machine | |
CN105090036A (en) | Air compressor waste heat secondary recycling device | |
CN107191906B (en) | Sintering flue gas waste heat recovery system | |
CN213699373U (en) | Full oil recovery system with multiple absorption towers operating in parallel | |
CN103147990A (en) | Air compressor waste heat recovery system | |
CN205980869U (en) | Oil smoke is heat exchange module for coolant tank | |
CN210645445U (en) | High-efficient infiltration type oil purifier |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
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: 20150325 Termination date: 20181020 |