CN203639488U - Combined heat exchanger - Google Patents
Combined heat exchanger Download PDFInfo
- Publication number
- CN203639488U CN203639488U CN201320859217.9U CN201320859217U CN203639488U CN 203639488 U CN203639488 U CN 203639488U CN 201320859217 U CN201320859217 U CN 201320859217U CN 203639488 U CN203639488 U CN 203639488U
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- Prior art keywords
- heat exchange
- exchange unit
- temperature heat
- gas
- low
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- 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 - Lifetime
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- 239000007789 gas Substances 0.000 claims abstract description 116
- 239000003546 flue gas Substances 0.000 claims abstract description 28
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 27
- 239000003034 coal gas Substances 0.000 claims description 29
- 238000005452 bending Methods 0.000 claims description 4
- 238000009792 diffusion process Methods 0.000 claims description 4
- 239000010935 stainless steel Substances 0.000 claims description 4
- 229910001220 stainless steel Inorganic materials 0.000 claims description 4
- 229910000975 Carbon steel Inorganic materials 0.000 claims description 3
- 239000010962 carbon steel Substances 0.000 claims description 3
- 230000008676 import Effects 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 9
- 238000011084 recovery Methods 0.000 abstract description 2
- 239000002918 waste heat Substances 0.000 abstract description 2
- 230000000149 penetrating effect Effects 0.000 abstract 1
- 239000000463 material Substances 0.000 description 12
- 238000005260 corrosion Methods 0.000 description 9
- 230000007797 corrosion Effects 0.000 description 8
- 230000009286 beneficial effect Effects 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000003628 erosive effect Effects 0.000 description 2
- 239000003517 fume Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 208000011580 syndromic disease Diseases 0.000 description 2
- 230000003245 working effect Effects 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Air Supply (AREA)
Abstract
The utility model provides a combined heat exchanger, in particular to a combined heat exchanger in a flue gas waste heat recovery system of a medium-high temperature hot blast stove in the production of modern blast furnaces. The combined heat exchanger comprises a low-temperature heat exchange unit and a high-temperature heat exchange unit which are serially connected and communicated, a flue gas pipeline and a gas pipeline are arranged in the low-temperature heat exchange unit and the high-temperature heat exchange unit in a penetrating mode, a flue gas inlet is formed in one side, located in the high-temperature heat exchange unit, of the flue gas pipeline, a gas inlet is formed in one side, located in the low-temperature heat exchange unit, of the gas pipeline, the flowing direction of flue gas in the flue gas pipeline is that high-temperature flue gas flows to the low-temperature heat exchange unit from the high-temperature heat exchange unit, and the flowing. The utility model discloses a can improve heat exchange efficiency, can prolong equipment life again, practice thrift cost and simple to operate, the little combination formula heat exchanger of area.
Description
Technical field
The utility model relates to a kind of interchanger, particularly a kind of unitized exchanger in high-blast-temperature hot-blast stove flue gas waste heat recovery system in modern blast furnace production.
Background technology
Hot-blast stove fume residual neat recovering system is mainly that the flue gas that utilizes hotblast stove to produce will enter the heat-exchange system that the coal gas of hotblast stove carries out preheating.At present, the interchanger that hot-blast stove fume residual neat recovering system uses mainly contains two kinds: heat-pipe heat exchanger and plate-type heat exchanger.
Heat-pipe heat exchanger temperature range and hotblast stove working condition adapt, invest less, generally can be by gas preheating to 180 ℃ left and right.But the heat pipe of heat-pipe heat exchanger easily lost efficacy, the life-span is short, thermo-efficiency is low, when excess Temperature, can cause booster.
Plate-type heat exchanger can be by gas preheating to higher temperature (more than 200 ℃), and heat transfer coefficient is high, erosion resistant, and overload capacity is strong, and the life-span is longer than hot tube heat exchanger; But under identical flue gas and coal gas condition, the drag losses of plate-type heat exchanger is larger, and facility investment is high, low-temperature zone is easily by the Cl in coal gas
-1corrosion, causes equipment breakage, and then causes gas leak, when serious, can cause gas explosion.Also there are some plate-type heat exchangers to adopt high temperature resistant and corrosion-resistant material manufacture, but above-mentioned not only high temperature resistant but also corrosion-resistant material is very expensive, cause the cost of plate-type heat exchanger very high, lack economy, can not promote the use of on a large scale.
If by above-mentioned two kinds of simple arranged in series of interchanger in engineering, need to increase the facilities such as a set of valve, pipe connecting and instrument monitoring, it installs complicated, not only increase the floor space of equipment, also increased the resistance of gas flow in equipment, cause the loss of heat larger, can not play positively effect.
Utility model content
The purpose of this utility model is to provide one can improve heat exchange efficiency, again can the extension device life-span, and cost-saving and easy for installation, the unitized exchanger that floor space is few.
For achieving the above object, the utility model proposes a kind of unitized exchanger, wherein, described unitized exchanger comprises serial connection and connects the low-temperature heat exchange unit and the high temperature heat exchange unit that arrange, in described low-temperature heat exchange unit and described high temperature heat exchange unit, be all equipped with flue and gas line, a side that is positioned at described high temperature heat exchange unit at described flue is provided with gas approach, a side that is positioned at described low-temperature heat exchange unit at described gas line is provided with gas inlet, in described flue, the circulating direction of flue gas is that high-temperature flue gas flows to described low-temperature heat exchange unit from described high temperature heat exchange unit, in described gas line the circulating direction of coal gas be low temperature coal gas from described low-temperature heat exchange unit stream to described high temperature heat exchange unit.
Unitized exchanger as above, wherein, described gas line comprises:
Gas line low-temperature zone, is arranged in described low-temperature heat exchange unit;
Gas line high temperature section, is arranged in described high temperature heat exchange unit;
Gas line linkage section, connects described gas line high temperature section and described gas line low-temperature zone.
Unitized exchanger as above, wherein, described flue arranges in horizontal direction and runs through described low-temperature heat exchange unit and described high temperature heat exchange unit.
Unitized exchanger as above, wherein, in described low-temperature heat exchange unit, described gas line low-temperature zone is set in parallel in the top of described flue.
Unitized exchanger as above, wherein, in described high temperature heat exchange unit, described gas line high temperature section is bending setting, and the import of described gas line high temperature section and outlet are all arranged on the top of described high temperature heat exchange unit.
Unitized exchanger as above, wherein, the side that described gas line is positioned at described high temperature heat exchange unit is provided with gas exit, and described gas inlet and described gas exit are all connected with adapter bonnet.
Unitized exchanger as above, wherein, described gas inlet along continuous straight runs is offered and connected described adapter bonnet arranges in horizontal direction, and described gas exit is vertically offered and connected described adapter bonnet is vertical direction setting.
Unitized exchanger as above, wherein, is connected on the described adapter bonnet of described gas inlet and on described gas line linkage section and is provided with coal gas diffusion pipe.
Unitized exchanger as above, wherein, the side that described flue is positioned at described low-temperature heat exchange unit is provided with exhanst gas outlet, and described gas approach and described exhanst gas outlet are all connected with adapter bonnet.
Unitized exchanger as above, wherein, described low-temperature heat exchange unit is carbon steel low-temperature heat exchange unit, described high temperature heat exchange unit is stainless steel high temperature heat exchange unit.
Compared with prior art, the utlity model has following characteristics and advantage:
1, the unitized exchanger the utility model proposes, the temperature of coal gas, entering temperature before high temperature heat exchange unit higher than " dew point " temperature, has been avoided " the Cl in coal gas
-1" corrosion to high temperature heat exchange unit; and then high temperature heat exchange unit is only selected high temperature material manufacture; corrosion resistant material is selected in low-temperature heat exchange unit; according to the difference of different steps gas working parameter; in equipment, selected different heat exchange units; can overcome the resistant to elevated temperatures problem of material of high temperature heat exchange unit, can overcome again the corrosion resistant problem of material of low-temperature heat exchange unit, has greatly saved again production cost when increasing work-ing life of equipment.
2, the unitized exchanger the utility model proposes, its high temperature heat exchange unit can, by more than heated by gas to 200 ℃, be conducive to improve the theoretical combustion temperature of hotblast stove, enters stove wind-warm syndrome thereby improved, and has reduced the power consumption of ironmaking.
3, the unitized exchanger the utility model proposes, its high temperature heat exchange unit and the setting of low-temperature heat exchange units in series and be combined into an integral device, its air resistance is little, has greatly improved the efficiency of heat exchange, and its floor space is little, and installation aspect is also very convenient.
4, the unitized exchanger the utility model proposes, the flue gas that adopts hotblast stove to produce carries out preheating to coal gas, has also reduced the heat that flue gas is taken away when coal gas is carried out to preheating, can reach the object of energy-conserving and environment-protective.
Accompanying drawing explanation
Accompanying drawing described here is only for task of explanation, and limits never in any form the utility model scope of disclosure.In addition, shape and the proportional sizes etc. of the each parts in figure is only schematically, for helping understanding of the present utility model, is not shape and the proportional sizes that specifically limits the each parts of the utility model.Those skilled in the art, under instruction of the present utility model, can select various possible shapes and proportional sizes to implement the utility model as the case may be.
Fig. 1 is the structural representation of the utility model unitized exchanger.
10-low-temperature heat exchange unit; 20-high temperature heat exchange unit; 30-flue; 31-gas approach; 32-exhanst gas outlet; 40-gas line; 41-gas line low-temperature zone; 42-gas line high temperature section; 43-gas line linkage section; 44-gas inlet; 45-gas exit; 46-coal gas diffusion pipe; 100-unitized exchanger.
Embodiment
With the description of the utility model embodiment, can more be well understood to details of the present utility model by reference to the accompanying drawings.But embodiment of the present utility model described here,, for explaining the purpose of this utility model, is only to restriction of the present utility model and can not be understood as by any way.Under instruction of the present utility model, technician can conceive based on possible distortion arbitrarily of the present utility model, and these all should be regarded as belonging to scope of the present utility model.
Please refer to Fig. 1, is the structural representation of the utility model unitized exchanger.The high-temperature flue gas preheating gas that the unitized exchanger 100 the utility model proposes utilizes hotblast stove to produce, as shown in Figure 1, unitized exchanger 100, comprise serial connection and connect the low-temperature heat exchange unit 10 and the high temperature heat exchange unit 20 that arrange, low-temperature heat exchange unit 10 can be by gas preheating to more than " dew point " temperature (100～120 ℃), high temperature heat exchange unit 20 can be by more than gas preheating to 200 ℃, interior flue 30 and the gas line 40 of being all equipped with of low-temperature heat exchange unit 10 and high temperature heat exchange unit 20, a side that is positioned at high temperature heat exchange unit 20 at flue 30 is provided with gas approach 31, a side that is positioned at low-temperature heat exchange unit 10 at gas line 40 is provided with gas inlet 44, the circulating direction of flue 30 interior flue gases is that high-temperature flue gas flows to low-temperature heat exchange unit 10 from high temperature heat exchange unit 20, the circulating direction of gas line 40 interior coal gas is that low temperature coal gas flows to high temperature heat exchange unit 20 from low-temperature heat exchange unit 10.
Working process of the present utility model is, first, need the low temperature coal gas of preheating to enter low-temperature heat exchange unit 10 through gas inlet 44, and first the high-temperature flue gas that hotblast stove produces enters high temperature heat exchange unit 20 through gas approach 31, high-temperature flue gas first carries out a heat exchange and changes low-temperature flue gas in high temperature heat exchange unit 20; This low-temperature flue gas enters low-temperature heat exchange unit 10 low temperature coal gas is wherein carried out to preheating for the first time, and low temperature coal gas is preheating to " dew point " temperature and changes above coal gas of high temperature into; Afterwards, the coal gas of high temperature of temperature more than " dew point " enters high temperature heat exchange unit 20 again, and the high-temperature flue gas being produced by hotblast stove in high temperature heat exchange unit 20 carries out preheating for the second time and is heated to more than 200 ℃.From above-mentioned working process of the present utility model, the temperature of coal gas, entering temperature before high temperature heat exchange unit 20 higher than " dew point " temperature (100～120 ℃), has been avoided " the Cl in coal gas
-1" corrosion to high temperature heat exchange unit; and then high temperature heat exchange unit 20 is only selected high temperature material manufacture; corrosion resistant material is selected in low-temperature heat exchange unit 10; like this; according to the difference of different steps gas working parameter, has selected different heat exchange units in equipment, can overcome the resistant to elevated temperatures problem of material of high temperature heat exchange unit 20; can overcome again the corrosion resistant problem of material of low-temperature heat exchange unit 10, has greatly saved again production cost when increasing work-ing life of equipment.And high temperature heat exchange unit 20 can, by more than heated by gas to 200 ℃, be conducive to improve the theoretical combustion temperature of hotblast stove, enters stove wind-warm syndrome thereby improved, and has reduced the power consumption of ironmaking.Meanwhile, because high temperature heat exchange unit 20 and low-temperature heat exchange unit 10 series connection settings are combined into an integral device, its air resistance is little, has greatly improved the efficiency of heat exchange, and its floor space is little, installs also very convenient.Finally, the flue gas that the utility model adopts hotblast stove to produce carries out preheating to coal gas, has also reduced the heat that flue gas is taken away when coal gas is carried out to preheating, can reach the object of energy-conserving and environment-protective.
In the utility model, gas line 40 comprises gas line low-temperature zone 41, gas line high temperature section 42 and gas line linkage section 43.Wherein, gas line low-temperature zone 41 is arranged in low-temperature heat exchange unit 10, and gas line high temperature section 42 is arranged in high temperature heat exchange unit 20, and gas line linkage section 43 connects gas line high temperature section 41 and gas line low-temperature zone 42.Gas line linkage section 43 is syphon shape, is beneficial to flowing of coal gas.Those skilled in the art also can be designed to gas line linkage section 43 to be beneficial to other shapes of flow of gas.
In the utility model, flue 30 arranges in horizontal direction and runs through low-temperature heat exchange unit 10 and high temperature heat exchange unit 20.Said structure meets the flow characteristics of flue gas, is beneficial to flue gas flowing and thermal exchange in interchanger 100.
Further, in low-temperature heat exchange unit 10, gas line low-temperature zone 41 is set in parallel in the top of flue 30.Like this, both guaranteed that gas line low-temperature zone 41 and flue 30 have certain contact area to carry out thermal exchange, can make again gas line 40 and flue 30 have less air resistance.Meanwhile, horizontally disposed gas line low-temperature zone 41 does not have bending, can further avoid water droplet on wall, to condense therein yet, has played certain etch-proof effect.
Further, in high temperature heat exchange unit 20, gas line high temperature section 42 is bending setting, and the import of gas line high temperature section 42 and outlet are all arranged on the top of high temperature heat exchange unit 20.So just, increased the contact area of operation length and gas line high temperature section 42 and the flue 30 of gas line high temperature section 42, having realized coal gas fully heats at the interior quilt in heat unit 20, to guarantee that the gas temperature after 20 heating of heat unit reaches more than 200 ℃, the final temperature of combustion that improves hotblast stove, reduces the energy consumption of smelting iron.
Further, the side that gas line 40 is positioned at high temperature heat exchange unit 20 arranges gas exit 45, and the side that flue 30 is positioned at low-temperature heat exchange unit 10 is provided with exhanst gas outlet 32, and gas inlet 44 and gas exit 45 are all connected with adapter bonnet; Gas approach 31 and exhanst gas outlet 32 are also all connected with adapter bonnet; So that being connected of gas line 40 and flue 30 and other pipelines.
Further, gas inlet 44 along continuous straight runs are offered and the adapter bonnet that is connected with gas inlet 44 also arranges in horizontal direction, and gas exit 45(is the outlet of gas line high temperature section 42) vertically offer and the adapter bonnet that is connected with gas exit 45 is vertical direction setting.
Further, be connected on the adapter bonnet of gas inlet 44 and on gas line linkage section 43 and be provided with and be with valvular coal gas diffusion pipe 46, under special circumstances coal gas is discharged.
In the utility model, low-temperature heat exchange unit 10 is the carbon steel low-temperature heat exchange unit that formed by the manufacture of plain carbon stool material, has erosion resistance; The stainless steel high temperature heat exchange unit of high temperature heat exchange unit 20 for being formed by the manufacture of common stainless steel material, can be high temperature resistant.
For the detailed explanation of the respective embodiments described above, its object is only the utility model to make an explanation, so that can understand better the utility model, but, it is to restriction of the present utility model that these descriptions can not be construed to any reason, particularly, also arbitrary combination mutually of each feature of describing in different embodiments, thereby form other embodiments, except there being clearly contrary description, these features should be understood to can be applied in any one embodiment, and are also not only confined to described embodiment.
Claims (10)
1. a unitized exchanger, it is characterized in that, described unitized exchanger comprises serial connection and connects the low-temperature heat exchange unit and the high temperature heat exchange unit that arrange, in described low-temperature heat exchange unit and described high temperature heat exchange unit, be all equipped with flue and gas line, a side that is positioned at described high temperature heat exchange unit at described flue is provided with gas approach, a side that is positioned at described low-temperature heat exchange unit at described gas line is provided with gas inlet, in described flue, the circulating direction of flue gas is that high-temperature flue gas flows to described low-temperature heat exchange unit from described high temperature heat exchange unit, in described gas line the circulating direction of coal gas be low temperature coal gas from described low-temperature heat exchange unit stream to described high temperature heat exchange unit.
2. unitized exchanger as claimed in claim 1, is characterized in that, described gas line comprises:
Gas line low-temperature zone, is arranged in described low-temperature heat exchange unit;
Gas line high temperature section, is arranged in described high temperature heat exchange unit;
Gas line linkage section, connects described gas line high temperature section and described gas line low-temperature zone.
3. unitized exchanger as claimed in claim 2, is characterized in that, described flue arranges in horizontal direction and runs through described low-temperature heat exchange unit and described high temperature heat exchange unit.
4. unitized exchanger as claimed in claim 3, is characterized in that, in described low-temperature heat exchange unit, described gas line low-temperature zone is set in parallel in the top of described flue.
5. unitized exchanger as claimed in claim 2 or claim 3, it is characterized in that, in described high temperature heat exchange unit, described gas line high temperature section is bending setting, and the import of described gas line high temperature section and outlet are all arranged on the top of described high temperature heat exchange unit.
6. unitized exchanger as claimed in claim 2, is characterized in that, the side that described gas line is positioned at described high temperature heat exchange unit is provided with gas exit, and described gas inlet and described gas exit are all connected with adapter bonnet.
7. unitized exchanger as claimed in claim 6, it is characterized in that, described gas inlet along continuous straight runs is offered and connected described adapter bonnet arranges in horizontal direction, and described gas exit is vertically offered and connected described adapter bonnet is vertical direction setting.
8. the unitized exchanger as described in claim 6 or 7, is characterized in that, is connected on the described adapter bonnet of described gas inlet and on described gas line linkage section and is provided with coal gas diffusion pipe.
9. unitized exchanger as claimed in claim 3, is characterized in that, the side that described flue is positioned at described low-temperature heat exchange unit is provided with exhanst gas outlet, and described gas approach and described exhanst gas outlet are all connected with adapter bonnet.
10. unitized exchanger as claimed in claim 1, is characterized in that, described low-temperature heat exchange unit is carbon steel low-temperature heat exchange unit, and described high temperature heat exchange unit is stainless steel high temperature heat exchange unit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320859217.9U CN203639488U (en) | 2013-12-24 | 2013-12-24 | Combined heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320859217.9U CN203639488U (en) | 2013-12-24 | 2013-12-24 | Combined heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203639488U true CN203639488U (en) | 2014-06-11 |
Family
ID=50870750
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320859217.9U Expired - Lifetime CN203639488U (en) | 2013-12-24 | 2013-12-24 | Combined heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203639488U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103695587A (en) * | 2013-12-24 | 2014-04-02 | 中冶京诚工程技术有限公司 | Combined heat exchanger |
| CN110982976A (en) * | 2020-01-06 | 2020-04-10 | 宝钢湛江钢铁有限公司 | Plate type gas-gas heat exchanger |
| CN111647703A (en) * | 2020-07-08 | 2020-09-11 | 中冶赛迪工程技术股份有限公司 | Combined type coal gas preheating system and method |
-
2013
- 2013-12-24 CN CN201320859217.9U patent/CN203639488U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103695587A (en) * | 2013-12-24 | 2014-04-02 | 中冶京诚工程技术有限公司 | Combined heat exchanger |
| CN110982976A (en) * | 2020-01-06 | 2020-04-10 | 宝钢湛江钢铁有限公司 | Plate type gas-gas heat exchanger |
| CN111647703A (en) * | 2020-07-08 | 2020-09-11 | 中冶赛迪工程技术股份有限公司 | Combined type coal gas preheating system and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140611 |