CN205825099U - A kind of pressure-variable adsorption oxygen-enriched burning device - Google Patents
A kind of pressure-variable adsorption oxygen-enriched burning device Download PDFInfo
- Publication number
- CN205825099U CN205825099U CN201620681224.8U CN201620681224U CN205825099U CN 205825099 U CN205825099 U CN 205825099U CN 201620681224 U CN201620681224 U CN 201620681224U CN 205825099 U CN205825099 U CN 205825099U
- Authority
- CN
- China
- Prior art keywords
- air
- oxygen
- gas
- air inlet
- combustor
- 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
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Landscapes
- Separation Of Gases By Adsorption (AREA)
Abstract
The utility model discloses a kind of pressure-variable adsorption oxygen-enriched burning device, including pressure swing adsorption oxygen and combustor, also include aerator, air filter, air heating apparatus, gas-liquid separator and carbon dioxide adsorption device, the air inlet of pressure swing adsorption oxygen connects air filter, the air inlet of air filter connects aerator, the gas outlet of pressure swing adsorption oxygen is connected to the inlet of cold air of air heating apparatus, the hot air outlet of air heating apparatus connects the air inlet of gas-liquid separator, the gas outlet of gas-liquid separator is connected to the air inlet of combustor, the exhaust opening of combustor connects carbon dioxide adsorption device, the gas outlet of carbon dioxide adsorption device is connected to the air inlet of aerator.Compared with prior art, this utility model, by the oxygen heating laggard row gas-liquid separation prepared by negative-pressure adsorption oxygenerator, makes pure oxygen enter combustor, and collects the oxygen not participating in combustion reaction, and this utility model simple in construction saves the energy.
Description
Technical field
This utility model relates to Thermal Power Engineering Field, particularly a kind of pressure-variable adsorption oxygen-enriched burning device.
Background technology
Oxygen-enriched combusting is that the gaseous mixture utilizing air to separate the pure oxygen obtained and a part of boiler exhaust composition replaces air
Oxidant when doing fossil-fuel-fired, this combustion system can make flue gas CO2 at concentrations up to more than 85%, can divide
From and by most flue gas direct liquefaction recycle, the recovery of beneficially CO2, can effectively reduce the row of greenhouse gases
Putting, oxygen-enriched combusting can also effectively reduce the discharge of the pollutant such as NOX and SO2 in addition, is an energy-efficient combustion system.
Oxygen-enriched combustion technology, all has application in glass industry, metallurgical industry and Thermal Power Engineering Field at present.
The oxygen-enriched burning device of prior art prepare oxygen-enriched after be generally required for carrying out heating oxygen-enriched, such energy
Enough improve oxygen-enriched temperature, and oxygen-enriched in moisture can become steam, if the steam in oxygen-enriched is not removed, oxygen-enriched enter
In entering combustor and after full combustion of fuel, after combustor cooling, in it, moisture can be left;And due to oxygen-enriched be continually
Ground enters combustor, it will usually cause oxygen excess, and the oxygen of excess does not the most participate in combustion reaction, and result is with flue gas one piece row
Go out, cause the biggest waste.
Summary of the invention
The purpose of this utility model is intended to solve the deficiency of prior art problem, it is provided that a kind of pressure-variable adsorption oxygen-enriched combusting dress
Put.
For reaching above-mentioned purpose, this utility model is implemented according to techniques below scheme:
A kind of pressure-variable adsorption oxygen-enriched burning device, including pressure swing adsorption oxygen and combustor, also includes aerator, air
Filter, air heating apparatus, gas-liquid separator and carbon dioxide adsorption device, the air inlet of described pressure swing adsorption oxygen is even
Connecing air filter, the air inlet of air filter connects aerator, and the gas outlet of described pressure swing adsorption oxygen is connected to sky
The inlet of cold air of gas heater, the hot air outlet of air heating apparatus connects the air inlet of gas-liquid separator, and gas-liquid is divided
Be connected to the air inlet of combustor from the gas outlet of device, the exhaust opening of described combustor connects carbon dioxide adsorption device, and two
The gas outlet of carbonoxide adsorbent equipment is connected to the air inlet of aerator.
Further, in order to reduce oxygen-enriched waste, in the air inlet of described combustor, it is provided with back-pressure valve, enters combustion when oxygen-enriched
After burning indoor, the pressure in combustor is gradually increased, until the completely rear back-pressure valve of the oxygen-enriched collection in combustor can stop oxygen-enriched
It is again introduced into.
Preferably, described air heating apparatus is pipe heat exchanger.
Compared with prior art, pressure-variable adsorption oxygen-enriched burning device of the present utility model, by by negative-pressure adsorption oxygenerator
The oxygen heating laggard row gas-liquid separation prepared, makes pure oxygen enter combustor, and combustor is discharged flue gas and do not participates in combustion
The oxygen of burning reaction is again passed through in pressure swing adsorption oxygen after carbon dioxide adsorption device removes carbon dioxide and collects not
Participate in the oxygen of combustion reaction, this utility model simple in construction, save the energy.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
Below in conjunction with the accompanying drawings and this utility model is further described by specific embodiment, in the signal of this utility model
Property embodiment and explanation be used for explaining this utility model, but be not intended as restriction of the present utility model.
A kind of pressure-variable adsorption oxygen-enriched burning device as shown in Figure 1, including pressure swing adsorption oxygen 3 and combustor 7, also wraps
Include aerator 1, air filter 2, air heating apparatus 4, gas-liquid separator 5 and carbon dioxide adsorption device 8, wherein, air
Heater 4 is pipe heat exchanger, and the air inlet of described pressure swing adsorption oxygen 3 connects air filter 2, air filter 2
Air inlet connect aerator 1, the gas outlet of described pressure swing adsorption oxygen 3 is connected to the inlet of cold air of pipe heat exchanger,
The hot air outlet of pipe heat exchanger connects the air inlet of gas-liquid separator 5, and the gas outlet of gas-liquid separator 5 is connected to combustor
The air inlet of 7, is provided with back-pressure valve 6 in the air inlet of combustor 7, the exhaust opening of described combustor 6 connects carbon dioxide adsorption
Device 8, carbon dioxide adsorption device 8 is built with the adsorbent for absorbing carbon dioxide, giving vent to anger of carbon dioxide adsorption device 8
Mouth is connected to the air inlet of aerator 1.
The technical solution of the utility model is not limited to the restriction of above-mentioned specific embodiment, every according to skill of the present utility model
The technology deformation that art scheme is made, within each falling within protection domain of the present utility model.
Claims (3)
1. a pressure-variable adsorption oxygen-enriched burning device, including pressure swing adsorption oxygen and combustor, it is characterised in that: also include drum
Blower fan, air filter, air heating apparatus, gas-liquid separator and carbon dioxide adsorption device, described pressure swing adsorption oxygen
Air inlet connect air filter, the air inlet of air filter connects aerator, giving vent to anger of described pressure swing adsorption oxygen
Mouth is connected to the inlet of cold air of air heating apparatus, and the hot air outlet of air heating apparatus connects the air inlet of gas-liquid separator
Mouthful, the gas outlet of gas-liquid separator is connected to the air inlet of combustor, and the exhaust opening of described combustor connects has carbon dioxide to inhale
Adsorption device, the gas outlet of carbon dioxide adsorption device is connected to the air inlet of aerator.
Pressure-variable adsorption oxygen-enriched burning device the most according to claim 1, it is characterised in that: in the air inlet of described combustor
It is provided with back-pressure valve.
Pressure-variable adsorption oxygen-enriched burning device the most according to claim 1, it is characterised in that: described air heating apparatus is pipe
Formula heat exchanger.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620681224.8U CN205825099U (en) | 2016-07-01 | 2016-07-01 | A kind of pressure-variable adsorption oxygen-enriched burning device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620681224.8U CN205825099U (en) | 2016-07-01 | 2016-07-01 | A kind of pressure-variable adsorption oxygen-enriched burning device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN205825099U true CN205825099U (en) | 2016-12-21 |
Family
ID=57566718
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201620681224.8U Expired - Fee Related CN205825099U (en) | 2016-07-01 | 2016-07-01 | A kind of pressure-variable adsorption oxygen-enriched burning device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN205825099U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113983464A (en) * | 2021-09-26 | 2022-01-28 | 东北大学 | Combustion apparatus |
-
2016
- 2016-07-01 CN CN201620681224.8U patent/CN205825099U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113983464A (en) * | 2021-09-26 | 2022-01-28 | 东北大学 | Combustion apparatus |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103953921B (en) | Oxygen-enriched combustion boiler system and operation method thereof | |
CN105114945A (en) | Boiler system and flue gas and air system thereof | |
CN106669379A (en) | Boiler flue gas recirculation dehumidification device | |
CN2771659Y (en) | Device for reutilizing and purifying waste smoke of coal-burning boiler | |
CN205825099U (en) | A kind of pressure-variable adsorption oxygen-enriched burning device | |
CN105509037A (en) | Flue gas and air system for oxygen-enriched combustion and boiler system | |
CN107883780A (en) | A kind of wet process of FGD white cigarette controlling device | |
CN102588996B (en) | Oxygen-enriched combustion system | |
CN101655279A (en) | Multi-stage rotating energy-saving dust and harmful substance removing vertical boiler | |
CN106439876B (en) | The flue gas processing device and boiler system of boiler system | |
CN201170547Y (en) | Oxygenation combustion-supporting device for fire coal electrification boiler of circulating fluid bed | |
CN204693390U (en) | A kind of coal-burning boiler suppressing discharged nitrous oxides | |
CN204494467U (en) | A kind of novel energy-saving environment-friendly flame furnace system | |
CN104132372B (en) | A kind of burner of high-efficient energy-saving environment friendly | |
CN106500120A (en) | The low nitrogen of one kind preheating humidification and flue gas depth residual neat recovering system | |
CN207763512U (en) | A kind of wet process of FGD white cigarette controlling device | |
CN102494320B (en) | Coal-fired refrigerating boiler | |
CN205014344U (en) | Boiler system and flue gas air system thereof | |
CN206724466U (en) | A kind of energy-saving, environmental protection boiler of thermal protection | |
CN205746795U (en) | Combustion coal chain boiler low oxygen and low nitrogen burner | |
CN202328891U (en) | Coal refrigerating boiler | |
CN203768013U (en) | Environment-friendly oxygen generation combustion support system capable of reducing nitrogen oxide emission | |
CN205299590U (en) | Oxygen -enriched combustion system | |
CN206556252U (en) | A kind of condensed type combustion gas water heater of low NOx combustion | |
CN205807465U (en) | Mixed air distribution device of module furnace |
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 |
Granted publication date: 20161221 Termination date: 20210701 |
|
CF01 | Termination of patent right due to non-payment of annual fee |