CN2569084Y - LPG water-cooled heat exchanger - Google Patents
LPG water-cooled heat exchanger Download PDFInfo
- Publication number
- CN2569084Y CN2569084Y CN 02252532 CN02252532U CN2569084Y CN 2569084 Y CN2569084 Y CN 2569084Y CN 02252532 CN02252532 CN 02252532 CN 02252532 U CN02252532 U CN 02252532U CN 2569084 Y CN2569084 Y CN 2569084Y
- Authority
- CN
- China
- Prior art keywords
- liquefied petroleum
- petroleum gas
- cooling water
- frame structure
- channel
- 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
Links
- 239000003915 liquefied petroleum gas Substances 0.000 claims abstract description 74
- 239000000498 cooling water Substances 0.000 claims abstract description 60
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims abstract description 17
- 239000010936 titanium Substances 0.000 claims abstract description 3
- 229910052719 titanium Inorganic materials 0.000 claims abstract description 3
- 229910052751 metal Inorganic materials 0.000 claims abstract 8
- 239000002184 metal Substances 0.000 claims abstract 8
- 239000010410 layer Substances 0.000 claims description 22
- 239000011229 interlayer Substances 0.000 claims description 6
- 238000013461 design Methods 0.000 abstract description 9
- 238000002955 isolation Methods 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 7
- 239000003208 petroleum Substances 0.000 description 5
- 238000004891 communication Methods 0.000 description 4
- 230000007797 corrosion Effects 0.000 description 3
- 238000005260 corrosion Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000002826 coolant Substances 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 230000008676 import Effects 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 230000001154 acute effect Effects 0.000 description 1
- 239000007767 bonding agent Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229930183489 erectone Natural products 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Images
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
A water-cooled heat exchanger for liquefied petroleum gas is characterized by that the liquefied petroleum gas which is compressed by cracker and then fed into tower tank is separated into negative temp. and then heated by heat exchange, and fed into ball tank for storage at proper temp., it is mainly characterized by that two sides of several frame bodies are respectively equipped with cooling water channel and liquefied petroleum gas channel, then the frame bodies are stacked up and down, between every frame bodies a titanium metal plate with through hole is stuck, the frame bodies are used as isolation layers among all layers of frame bodies and form a heat exchange circulation chamber, and the frame bodies are alternately stacked and arranged to form a liquefied petroleum gas circulation layer and a cooling water circulation layer by matching with the design of a channel, and the large-area chamber contact and the layer-by-layer heat exchange are utilized, the liquefied petroleum gas can be heated quickly and effectively, the cooling water and the liquefied petroleum gas can be isolated in respective independent circulation layers, and the purposes of easy assembly, safety and practicability are achieved.
Description
Technical field
The utility model relates to a kind of closed not contaminated and liquefied petroleum gas water-cooled heat exchanger with high heat exchange rate simple in structure.
Background technology
Liquefied petroleum gas (Liquefied Petroleum Gas is called for short LPG) is the product behind the light oil cracking, after finishing cracking, be-45 ℃ stable liquid state, and the general trough for used balls of the mode of its storage is stored, under the normal temperature state, if-45 ℃ liquefied petroleum gas directly enters the ball groove, the temperature difference that it is acute excessively, to make the structure of ball groove because of sharply expanding with heat and contract with cold, and cause producing the crack, and then cause the leakage of liquefied petroleum gas, this has sizable threat to public safety, therefore before liquefied petroleum gas enters the ball groove of storage, all can pass through the processing that heats up earlier, with the temperature difference of shortening with the ball groove, and the processing that heats up generally is with heat exchanger liquefied petroleum gas to be warming up to about about 4 ℃, so just can guarantee the safety of ball groove structure.
See also Fig. 1, the heat exchanger that present liquefied petroleum gas more generally adopts is to feed liquefied petroleum gas with an inlet tube 1, on inlet tube 1, be communicated with several circuitous manifolds 2 again, send liquefied petroleum gas with outlet 3 more at last, cooling water is then sprayed the outside of body by the top in the shower mode, in order to increase the area that contacts with cooling water, each manifold 2 sets up in circuitous mode of twining, and reaches the purpose of cold and hot exchange.When the outside sprinkling of body cooling water, squirt near zone in order to prevent that cooling water is excessive, need to erect one around interchanger partition wall 4, this kind mode is not only installed comparatively trouble, and the efficient of its heat exchange is also not good, and the intensity of manifold 2 more seems not enough because of caliber is less, because manifold 2 is exposed, thus be vulnerable to the external pollution corrosion, and when maintenance, therefore manifold 2 remains to be improved because of circuitous winding also is difficult for doing maintenance of clean-up.
Summary of the invention
The purpose of this utility model is in order to overcome the deficiencies in the prior art, to utilize applicant's working experience for many years, through continuous research and design, develops a kind of simple and convenient assembly eventually and has the enclosed liquefied petroleum gas water-cooled heat exchanger of high heat exchange rate.
The utility model is realized as follows:
The utility model is to be on the deckle board of frame structure body both sides of permeable type at several upper and lower surfaces, offer cooling-water duct and liquefied petroleum gas passage respectively, again that frame structure body is stacked up and down, and between each frame structure body, bind the titanium mesh that is provided with relative through hole, and upper and lower frames structure body is isolated, and make each frame structure body hollow part divide the circulation chamber that forms the top and bottom sealing, cooperate the design of titanium mesh lead to the hole site, can select to form circulation passage mutually with each layer frame structure body circulation chamber, and it is stacked in mode at interval, form cooling water circulation layer and liquefied petroleum air communication layer, last levels is sealed with bolt again, with each frame structure body of clamping; Like this, indoor the flowing to of flowing lumen that cooling water and liquefied petroleum gas can form at each frame structure body respectively exports discharge, and do cold and hot exchange in enclosed mode, so it can not spray the zone of spattering periphery with water, and the chamber that respectively circulates is positioned at internal body also can not be subjected to external pollution and weathering corrosion, reaches to be easy to dispose and the purpose of long service life.
The utility model also can pile up with a plurality of frame structure bodies and form, and between each layer frame structure body, bind titanium mesh, therefore its assembling is very easy, structural design is also comparatively simple, cooperate the design of through hole again, and make each layer form cooling water circulation layer and liquefied petroleum flow channel layer respectively, and cooling water circulation layer and liquefied petroleum air communication layer are runner independently separately in mode at interval, and do not have the situation of mixing, and then each self-forming circulation layer at interval.
The utility model is can also be with frame structure body stacked and isolate with titanium mesh, and make frame structure body hollow part form the circulation chamber, and do cold and hot exchange with the large tracts of land contact of circulation chamber, and has preferable heat exchange effect, and make different circulation layers with interval mode, and make circulation chamber top and bottom do cold and hot exchange simultaneously, improve the effect of heat exchange more.
Description of drawings
Below in conjunction with accompanying drawing the utility model is described further:
Fig. 1 is a habit formula heat exchanger schematic diagram
Fig. 2-the 1st, the external sight schematic diagram of the utility model cooling water frame structure
Fig. 2-the 2nd, the A-A cutaway view of Fig. 2-1
Fig. 2-the 3rd, the B-B cutaway view of Fig. 2-1
Fig. 3-the 1st, the external sight schematic diagram of the utility model liquefied petroleum gas frame structure
Fig. 3-the 2nd, the C-C cutaway view of Fig. 3-1
Fig. 3-the 3rd, the D-D cutaway view of Fig. 3-1
Fig. 4 is an assembling schematic diagram of the present utility model
Fig. 5 is the utility model liquefied petroleum air communication layer schematic diagram
Fig. 6 is the utility model cooling water circulation layer schematic diagram
Fig. 7 is the utility model schematic appearance
Fig. 8 is the utility model heat exchange circulation schematic diagram
Among the figure
Commonly use partly:
1 inlet tube, 2 manifolds, 3 outlets, 4 partition walls;
The utility model part:
10,10 ' frame structure body, 11 hollow parts, 12, deckle board, 13,13 ' cooling-water duct, 14 liquefied petroleum gas passages, 15,15 ' conduit, 16 conduits, 17,17 ' circulation chamber;
20,20 ' frame structure body, 21 hollow parts, 22 deckle boards, 23 cooling-water ducts, 24,24 ' liquefied petroleum gas passage, 25,25 conduits, 26 conduits, 27,27 ' circulation chamber,
30 times seats, 31 liquefied petroleum gas imports, 32 coolant outlets, 33 flanges;
40,40 ' titanium mesh, 41,41 ' through hole, 42,42 ' through hole;
50 seats of honour, the outlet of 51 liquefied petroleum gas, 52 cooling water inlets, 53 flanges;
60 bolts.
The specific embodiment
See also Fig. 2-1, Fig. 2-2, Fig. 2-3, the frame structure body 10 of the utility model cooling water circulation layer is one to have the deckle board 12 of hollow part 11, offer the cooling-water duct 13 and the liquefied petroleum gas passage 14 of perforation respectively in deckle board 12 both sides, on cooling-water duct 13, laterally offer conduit 15,16 in addition, then do not have the conduit of offering in the position of liquefied petroleum gas passage 14.See also Fig. 3-1, Fig. 3-2, Fig. 3-3, the frame structure body 20 of the utility model liquefied petroleum air communication layer is one to have the deckle board 22 of hollow part 21, offer the cooling-water duct 23 and the liquefied petroleum gas passage 24 of perforation respectively in deckle board 22 both sides, on liquefied petroleum gas passage 24, laterally offer conduit 25,26 in addition, then do not have the conduit of offering in the position of cooling-water duct 23.See also Fig. 4, the utility model the time is to have the frame structure body 10 of mutual in regular turn stacked cooling water circulation on liquefied petroleum gas import 31 and coolant outlet 32 following 30 layer and the frame structure body 20 of liquefied petroleum gas one in assembling, and in 10,20 of two frame structure bodies, bind one deck titanium mesh 40 with bonding agent, therefore after each frame structure body 10,20 binds titanium mesh 40 up and down, will make hollow part 11,21 form the circulation chamber 17 of cooling water and the circulation chamber 27 of liquefied petroleum gas respectively.See also Fig. 4, Fig. 5, in order to make the liquefied petroleum gas in the subnatant liquefied oil gas circulation chamber 27, can be circulated in the circulation chamber 27 ' that is separated with one deck liquefied petroleum gas, through hole 41 is offered in position in titanium mesh 40 relative liquefied petroleum gas passages 24, and make that the liquefied petroleum gas in circulation chamber 27 is negotiable to the liquefied petroleum gas passage 14 of cooling water frame structure body 10, because there is no, the liquefied petroleum gas passage 14 on the cooling water frame structure body 10 offers the conduit that is communicated to cooling water flow cavity chamber 17, therefore liquefied petroleum gas is when being circulated to cooling water frame structure body 10, can't sneak into to cooling water flow cavity chamber 17, and only with its liquefied petroleum gas passage 14 as the path that is circulated to interlayer, the titanium mesh 40 ' of frame structure body 10 tops then offers through hole 41 ' relatively, so that the liquefied petroleum gas passage 14 of frame structure body 10 is communicated to the liquefied petroleum gas frame structure body 20 ' on upper strata, and then enter via liquefied petroleum gas passage 24 ' and conduit 25 ' in the circulation chamber 27 ' of liquefied petroleum gas.See also Fig. 4, Fig. 6, for the cooling water in the cooling water flow cavity chamber 17 that makes the upper strata can be circulated in the cooling water flow cavity chamber 17 ' of alternating floor, through hole 42 is offered in position in titanium mesh 40 relative cooling-water ducts 14, and make that the cooling water in circulation chamber 17 is negotiable to the cooling-water duct 23 of liquefied petroleum gas frame structure body 20, because there is no, the cooling-water duct 23 of liquefied petroleum gas frame structure body 20 offers the conduit that is communicated to liquefied petroleum gas circulation chamber 27, therefore cooling water is when being circulated to liquefied petroleum gas frame structure body 20, can't sneak into to liquefied petroleum gas circulation chamber 27, be as the path that is circulated to interlayer with cooling-water duct 23, the titanium mesh 40 ' of frame structure body 20 belows then also is provided with through hole 42 ' relatively, so that the cooling-water duct 23 of frame structure body 20 is communicated to the cooling water frame structure body 10 ' of lower floor, and then enter in the cooling water flow cavity chamber 17 ' via cooling-water duct 13 ' and conduit 15 '.See also Fig. 7, the utility model is in regular turn with frame structure body 10,20 mutual stacked and bonding titanium meshes 40, and on titanium mesh, cooperate the design of runner, select to offer corresponding through hole respectively at both sides, have the liquefied petroleum gas outlet 51 and cooling water inlet 52 seats of honour 50 in the superiors stacked again, and utilize flange 33,53 on the upper and lower seat 30,50 to wear bolt 60 to give sealedly, and press each frame structure body 10,20 of folder, make it more firmly stacked with upper and lower seat 30,50; The utility model utilizes modularity frame structure body 10,20, cooperates the design of titanium mesh 40 lead to the hole site, and is very easy in the feasible assembling, and structure is also comparatively simple, therefore can significantly reduce the cost of equipment.Fig. 8, the utility model utilizes frame structure body 10,20 and the design of collocation titanium mesh 40 through hole correspondence positions, can make cooling water be injected into cooling water flow cavity chamber 17 by the top, pass to next interlayer circulation chamber 17 by other effluent again, liquefied petroleum gas then is injected into liquefied petroleum gas circulation chamber 27 by the below, be circulated to last interlayer circulation chamber 27 by opposite side again, and the circulation layer of the circulation layer of each self-forming cooling water and liquefied petroleum gas, so do cold and hot exchange in enclosed mode, cooling water is not just understood the outer neighboring area that splashes equipment, and enclosed passage also is not subjected to external pollution and weathering corrosion, can improve service life of equipment, moreover, liquefied petroleum gas circulation chamber 27, its top and bottom all with large tracts of land contact cooling water flow cavity chamber 17, can effectively improve heat exchanger effectiveness, the liquefied petroleum gas of locating that makes outlet 51, certain rapidly intensification effect that reaches 4 ℃.
In sum, the utility model is the design of a dark tool practicality and progressive in fact, and does not see identical product and publication are arranged openly, thus meet the utility application condition, so file an application in accordance with the law.
Claims (5)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02252532 CN2569084Y (en) | 2002-09-04 | 2002-09-04 | LPG water-cooled heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02252532 CN2569084Y (en) | 2002-09-04 | 2002-09-04 | LPG water-cooled heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2569084Y true CN2569084Y (en) | 2003-08-27 |
Family
ID=33721990
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 02252532 Expired - Fee Related CN2569084Y (en) | 2002-09-04 | 2002-09-04 | LPG water-cooled heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2569084Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101305254B (en) * | 2005-09-14 | 2010-05-19 | 贝洱工业公司 | Heat exchanger |
| CN101297172B (en) * | 2005-09-16 | 2010-09-29 | 贝洱工业公司 | Plate heat exchanger, in particular charge air cooler |
| CN103270385A (en) * | 2010-11-08 | 2013-08-28 | 达纳加拿大公司 | Double baseplate oil cooler construction |
| CN112371852A (en) * | 2020-10-26 | 2021-02-19 | 湖州恒大液压设备有限公司 | Punch circulating internal cooling device of quick forging servo hydraulic machine |
-
2002
- 2002-09-04 CN CN 02252532 patent/CN2569084Y/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101305254B (en) * | 2005-09-14 | 2010-05-19 | 贝洱工业公司 | Heat exchanger |
| CN101297172B (en) * | 2005-09-16 | 2010-09-29 | 贝洱工业公司 | Plate heat exchanger, in particular charge air cooler |
| CN103270385A (en) * | 2010-11-08 | 2013-08-28 | 达纳加拿大公司 | Double baseplate oil cooler construction |
| CN103270385B (en) * | 2010-11-08 | 2016-08-10 | 达纳加拿大公司 | Double-basis leaf fat chiller configuration |
| CN112371852A (en) * | 2020-10-26 | 2021-02-19 | 湖州恒大液压设备有限公司 | Punch circulating internal cooling device of quick forging servo hydraulic machine |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |