CN204478088U - Residual-heat utilization device of incinerator - Google Patents
Residual-heat utilization device of incinerator Download PDFInfo
- Publication number
- CN204478088U CN204478088U CN201520067159.5U CN201520067159U CN204478088U CN 204478088 U CN204478088 U CN 204478088U CN 201520067159 U CN201520067159 U CN 201520067159U CN 204478088 U CN204478088 U CN 204478088U
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- CN
- China
- Prior art keywords
- import
- outlet
- low concentration
- combustion furnace
- gas
- 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
- 230000008676 import Effects 0.000 claims abstract description 39
- 239000007789 gas Substances 0.000 claims abstract description 29
- 238000002485 combustion reaction Methods 0.000 claims abstract description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 15
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000002912 waste gas Substances 0.000 claims abstract description 14
- 239000002699 waste material Substances 0.000 claims abstract description 9
- 239000003345 natural gas Substances 0.000 claims abstract description 7
- 239000007788 liquid Substances 0.000 claims abstract description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 4
- 239000001301 oxygen Substances 0.000 claims description 4
- 229910052760 oxygen Inorganic materials 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 9
- 239000012159 carrier gas Substances 0.000 abstract description 3
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 238000010438 heat treatment Methods 0.000 abstract description 2
- 239000002918 waste heat Substances 0.000 abstract description 2
- 229920006337 unsaturated polyester resin Polymers 0.000 description 8
- 238000005516 engineering process Methods 0.000 description 4
- 239000010808 liquid waste Substances 0.000 description 3
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 208000027418 Wounds and injury Diseases 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000011152 fibreglass Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 208000014674 injury Diseases 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
Abstract
The utility model discloses a kind of residual-heat utilization device of incinerator, it is characterized in that it includes combustion furnace (1), the bottom of combustion furnace (1) is provided with waste liquid import (2), low concentration gas import (3), high-concentration waste gas import (4) and natural gas combi inlet port (5), the outlet of combustion furnace (1) is connected with the import of workshop hot oil heater (7), the outlet of workshop hot oil heater (7) is connected with the import of low concentration gas preheating device (11), the outlet of low concentration gas preheating device (11) connects the import of water pre-heater apparatus (12), the import of the outlet connecting fan (6) of water pre-heater apparatus (12), the outlet of blower fan (6) is led to extraneous.The utility model is simple and practical, can utilize better the waste heat of combustion furnace, realizes the needs of Workshop Production heating, significantly reduces the Natural gas consumption of organic heat carrier gas fired-boiler, thus significantly reduces energy consumption cost.
Description
Technical field
The utility model relates to a kind of waste liquid waste gas combustion furnace exhaust-heat absorption and utilizes system.
Background technology
Unsaturated polyester resin technique functions comes from Sweden, after only improving and optimizing, is commercially produced in nineteen forty-one first by the U.S..And domesticly to start late, just started the production having small lot in 1958, after within 1966, Changzhou building materials 253 factory causes the production technology and eqUipment of unsaturated polyester resin from Britain, unsaturated polyester resin just starts commercialized development at home.Through the development of decades, be that the glass fiber reinforced plastics product of matrix penetrates into all trades and professions with unsaturated polyester resin, play a part more and more important in national economy every field.But generally speaking; the production technology of domestic unsaturated polyester resin also lags far behind advanced international standard; aspects such as being in particular in that production technology falls behind, being simply equipped, technical merit is low; rarely seen especially in environmental protection direction have larger input, and therefore domestic most unsaturated polyester resin manufacturer causes very large injury to surrounding enviroment.
Since entering 21st century, along with international environment consciousness is progressively strengthened, country has also put into effect relevant Environment Protection Policy in succession.Such severe situation forces domestic unsaturated polyester resin manufacturing enterprise investment construction plant process waste liquid, exhaust-gas treatment facilities in succession, wherein in the majority with waste liquid waste gas combustion furnace.Waste liquid waste gas combustion furnace relies on the advantages such as installation is simple to operate, the waste gas that disposes waste liquid is comparatively thorough to obtain the favor of a lot of unsaturated polyester resin manufacturing enterprise, but due to it, that organic-fuel must be used to carry out is combustion-supporting, thus causes its running use cost relatively large.
Summary of the invention
The purpose of this utility model is exactly for above-mentioned the deficiencies in the prior art, provides a kind of Natural gas consumption significantly reducing organic heat carrier gas fired-boiler, thus significantly reduces the residual-heat utilization device of incinerator of energy consumption cost.
For achieving the above object, the technical solution adopted in the utility model is as follows:
A kind of residual-heat utilization device of incinerator, it is characterized in that it includes combustion furnace, the bottom of combustion furnace is provided with waste liquid import, low concentration gas import, high-concentration waste gas import and natural gas combi inlet port, the outlet of combustion furnace is connected with the import of workshop hot oil heater, the outlet of workshop hot oil heater is connected with the import of low concentration gas preheating device, the outlet of low concentration gas preheating device connects the import of water pre-heater apparatus, the import of the outlet connecting fan of water pre-heater apparatus, the outlet of blower fan is led to extraneous.
Described workshop hot oil heater includes intervalve and is arranged on the chuck of intervalve outer wall, and the two ends of described intervalve connect the import of furnace exit and low concentration gas preheating device respectively.
Described low concentration gas preheating device includes intervalve and chuck, and this chuck is provided with preheating waste gas import and preheating waste gas outlet, and described preheating waste gas outlet is connected with described low concentration gas import.
Described water pre-heater apparatus includes intervalve and chuck, and this chuck is provided with water inlet and delivery port.
The exit of described blower fan is provided with determination of oxygen content instrument.
The beneficial effects of the utility model have:
Simple and practical, can utilize better the waste heat of combustion furnace, realize the needs of Workshop Production heating, significantly reduce the Natural gas consumption of organic heat carrier gas fired-boiler, thus significantly reduce energy consumption cost.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is done further
As shown in Figure 1, the utility model it include combustion furnace 1, the bottom of combustion furnace 1 is provided with waste liquid import 2, low concentration gas import 3, high-concentration waste gas import 4 and natural gas combi inlet port 5, the outlet of combustion furnace 1 is connected with the import of workshop hot oil heater 7, the outlet of workshop hot oil heater 7 is connected with the import of low concentration gas preheating device 11, the outlet of low concentration gas preheating device 11 connects the import of water pre-heater apparatus 12, the import of the outlet connecting fan 6 of water pre-heater apparatus 12, the outlet of blower fan 6 is led to extraneous.Described workshop hot oil heater 7 includes intervalve 8 and is arranged on the chuck 9 of intervalve 8 outer wall, the two ends of described intervalve 8 connect the import of combustion furnace 1 outlet and low concentration gas preheating device 11 respectively, the chuck of hot oil heater 7 is provided with heat conductive oil inlet and conduction oil outlet, and the conduction oil from workshop flows through and is heated from chuck.Described low concentration gas preheating device 11 structure also includes intervalve and chuck, this chuck is provided with preheating waste gas import and preheating waste gas outlet, preheating waste gas outlet is connected with low concentration gas import 3, and the low concentration gas of coming from workshop enters into combustion furnace 1 from low concentration gas import 3 again and burns after low concentration gas preheating device 11 preheating.From about 210 DEG C, workshop conduction oil through workshop hot oil heater 7 heat after, temperature reaches about 222 DEG C, flow to boiler afterwards and heats further, Workshop Production is used.The structure of described water pre-heater apparatus 12 also includes intervalve and chuck, and this chuck is provided with water inlet and delivery port, and the water after preheating is used as basin insulation and uses.
The exit of the utility model blower fan 6 can also arrange determination of oxygen content instrument 10, and determination of oxygen content instrument 10 controls the operation of blower fan 6, ensures combustion furnace 1 sufficient combustion, energy-saving and emission-reduction.Pass in low concentration gas import 3 be packaging time produce styrene and air, make full use of resource.
Other undeclared part that the utility model relates to is same as the prior art.
Claims (5)
1. a residual-heat utilization device of incinerator, it is characterized in that it includes combustion furnace (1), the bottom of combustion furnace (1) is provided with waste liquid import (2), low concentration gas import (3), high-concentration waste gas import (4) and natural gas combi inlet port (5), the outlet of combustion furnace (1) is connected with the import of workshop hot oil heater (7), the outlet of workshop hot oil heater (7) is connected with the import of low concentration gas preheating device (11), the outlet of low concentration gas preheating device (11) connects the import of water pre-heater apparatus (12), the import of the outlet connecting fan (6) of water pre-heater apparatus (12), the outlet of blower fan (6) is led to extraneous.
2. residual-heat utilization device of incinerator according to claim 1, it is characterized in that, it is characterized in that described workshop hot oil heater (7) includes intervalve (8) and is arranged on the chuck (9) of intervalve (8) outer wall, the two ends of described intervalve (8) connect the import of combustion furnace (1) outlet and low concentration gas preheating device (11) respectively.
3. residual-heat utilization device of incinerator according to claim 1, it is characterized in that described low concentration gas preheating device (11) includes intervalve and chuck, this chuck is provided with preheating waste gas import and preheating waste gas outlet, and described preheating waste gas outlet is connected with described low concentration gas import (3).
4. residual-heat utilization device of incinerator according to claim 1, it is characterized in that described water pre-heater apparatus (12) includes intervalve and chuck, this chuck is provided with water inlet and delivery port.
5. residual-heat utilization device of incinerator according to claim 1, is characterized in that the exit of described blower fan (6) is provided with determination of oxygen content instrument (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520067159.5U CN204478088U (en) | 2015-01-30 | 2015-01-30 | Residual-heat utilization device of incinerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520067159.5U CN204478088U (en) | 2015-01-30 | 2015-01-30 | Residual-heat utilization device of incinerator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204478088U true CN204478088U (en) | 2015-07-15 |
Family
ID=53633877
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520067159.5U Expired - Fee Related CN204478088U (en) | 2015-01-30 | 2015-01-30 | Residual-heat utilization device of incinerator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204478088U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104633676A (en) * | 2015-01-30 | 2015-05-20 | 宜兴市兴合树脂有限公司 | Incinerator waste heat utilization device |
| CN108800173A (en) * | 2018-07-11 | 2018-11-13 | 北京科技大学 | A kind of self-preheating type burner for the burning of low concentration combustible exhaust gas |
-
2015
- 2015-01-30 CN CN201520067159.5U patent/CN204478088U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104633676A (en) * | 2015-01-30 | 2015-05-20 | 宜兴市兴合树脂有限公司 | Incinerator waste heat utilization device |
| CN108800173A (en) * | 2018-07-11 | 2018-11-13 | 北京科技大学 | A kind of self-preheating type burner for the burning of low concentration combustible exhaust gas |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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: 20150715 |