CN209325791U - A kind of oil gas burner and oil vapor treatment system - Google Patents
A kind of oil gas burner and oil vapor treatment system Download PDFInfo
- Publication number
- CN209325791U CN209325791U CN201821685997.9U CN201821685997U CN209325791U CN 209325791 U CN209325791 U CN 209325791U CN 201821685997 U CN201821685997 U CN 201821685997U CN 209325791 U CN209325791 U CN 209325791U
- Authority
- CN
- China
- Prior art keywords
- gas
- oil
- oil gas
- burner
- air
- 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.)
- Active
Links
Landscapes
- Incineration Of Waste (AREA)
Abstract
The utility model discloses a kind of oil gas burners, including the combustion chamber being arranged along the vertical direction, it is connected with a gas mixer below the combustion chamber, there is a combustion head above combustion chamber, oil gas is mixed with air by gas mixer, and mixed gas is burnt in combustion head.It successively include the condensing unit condensed to oil gas, the gas-liquid separation unit separated to condensed oil gas and the burner that burning processing is carried out to remaining oil gas along oil gas travelling route the invention also discloses a kind of oil vapor treatment system using the oil gas burner.The advantages of oil gas burner disclosed by the utility model, is: by by oil gas disperse and come into full contact with oil gas with oxygen in air, in combustion head can full combustion, do not need additionally to add fuel, reduce processing cost.The advantages of oil vapor treatment system is: by the most of oil gas of condensing recovery, the irretrievable oil gas of small part is handled by burning, and efficiency of oil & gas processing is greater than 99.9%.
Description
Technical field
The utility model relates to the recycling of oil-containing exhaust gas and processing technology field more particularly to a kind of oil gas burner and
Gas recovery system for oil.
Background technique
Currently, mainly having absorption method, absorption process, condensation method, film process, combustion method etc. in petroleum vapor recovery processing method.This
A little methods there are petroleum vapor recovery low efficiency, concentration of oil and gas discharged is high, energy consumption is high, service life is low, cost of investment is high, security performance
The disadvantages of poor.
The waste that will lead to oil gas by burning processing oil gas is unfavorable for the recycling of oil gas, and needs in burning
It to add fuel additionally to ensure that oil gas is completely burned, also increase processing cost.
Utility model content
The technical problem to be solved by the utility model is to provide one kind not to need addition fuel energy completely burned oil
The burner of gas and the processing system for using the oil gas.
The utility model is to solve above-mentioned technical problem by the following technical programs:
A kind of oil gas burner is connected with a gas below the combustion chamber including the combustion chamber being arranged along the vertical direction
Body mixer, combustion chamber top have a combustion head, and oil gas is mixed with air by gas mixer, and mixed gas is in combustion head
Burning.
Preferably, the combustion head is with thickness and to cover the reticular structure of combustion chamber cross section, the combustion head energy
Enough external circuits heat entire reticular structure.
Preferably, it is additionally provided with gas distributor between gas mixer and combustion head, is evenly distributed on the gas distributor
There is through-hole for gas to pass through.
Preferably, the flue detector detected to the gas componant after burning is additionally provided with above combustion head.
A kind of oil vapor treatment system using the oil gas burner, along oil gas travelling route successively include to oil gas into
The condensing unit of row condensation, the gas-liquid separation unit separated to condensed oil gas and burning processing is carried out to remaining oil gas
Burner.
Preferably, the gas-liquid separation unit bottom is provided with catheter, and top is provided with the air guide being connected to adsorption tanks
Pipe.
Preferably, it is additionally provided between gas-liquid separation unit and burner and provides the first air inducing of oil gas for burner
Machine.
Preferably, the mixed cell of one Yu air communication are additionally provided between the first air-introduced machine and burner, it is described mixed
Closing has netted channel inside unit.
Preferably, between the mixed cell and burner and between the first air-introduced machine and gas-liquid separation unit respectively
It is provided with fire arrester.
Preferably, the inlet end of the burner, which is also connected with, provides the second air-introduced machine of air for burner.
The advantages of oil gas burner provided by the utility model, is: by will oil gas dispersion with air in make oil gas with
Oxygen comes into full contact with, in combustion head can full combustion, do not need additionally to add fuel, reduce processing cost.At oil gas
The advantages of reason system is: by the most of oil gas of condensing recovery, the irretrievable oil gas of small part is handled by burning, oil
Gas disposal efficiency is greater than 99.9%.
Detailed description of the invention
Fig. 1 is the schematic diagram of oil gas burner provided by the embodiments of the present invention；
Fig. 2 is the schematic diagram of combustion head provided by the embodiments of the present invention；
Fig. 3 is the schematic diagram of gas distributor provided by the embodiments of the present invention；
Fig. 4 is the schematic diagram of oil vapor treatment system provided by the embodiments of the present invention.
Specific embodiment
For the purpose of this utility model, technical solution and advantage is more clearly understood, below in conjunction with specific embodiment, and
Referring to attached drawing, the utility model is described in further detail.
As shown in Figure 1, a kind of oil gas burner, including the combustion chamber 11 being arranged along the vertical direction, 11 lower section of combustion chamber
Be connected with a gas mixer 12, there is a combustion head 13 above combustion chamber 11, oil gas after gas mixer 12 with air
It is mixed into combustion chamber 11, is then risen in combustion chamber 11 and carries out burning processing at combustion head 13.
With reference to Fig. 2, the combustion head 13 is with thickness and to cover the reticular structure of 11 cross section of combustion chamber, and oil gas is firing
It burns and is further dispersed at head 13, come into full contact with oil gas with oxygen, by external circuits to the netted knot of this combustion head 13
Structure is heated, thus the oil gas that ignites, the oil gas being dispersed throughout can the conflagration at combustion head 13, be not in a large amount of
Open fire improves safety.
In conjunction with Fig. 3, a gas distributor 14, the gas distribution are additionally provided between gas mixer 12 and combustion head 13
Through-hole 141 for gas to pass through is evenly equipped on device 14, thus by oil gas and the further dispersion mixing of air, the gas distributor
14 preferably reticular structure, gas distributors 14 can also prevent from being tempered.
Referring again to Fig. 1, the flue inspection detected to the gas componant after burning is additionally provided with above the combustion head 13
Device 15 is surveyed, so that it is guaranteed that tail gas meets discharge standard.
With reference to Fig. 4, the utility model additionally provides a kind of smoke processing system, successively includes to oil along oil gas travelling route
Condensing unit 2 that gas is condensed, the gas-liquid separation unit 3 that condensed oil gas is separated and remaining oil gas is fired
Burn the burner 1 of processing.
Oil gas enters in condensing unit 2 along pipeline, and most of oil gas is liquefied；Condensed oil gas enters gas-liquid separation
In unit 3, liquefied oil gas and remaining Oil-gas Separation；Remaining oil gas enters along pipeline is burned processing in burner 1；From
And complete the taking back and process of oil gas.
3 bottom of gas-liquid separation unit is provided with catheter 31, and top is provided with the gas-guide tube being connected to adsorption tanks 1
32；Liquid is flowed out from catheter 31, and gas enters adsorption tanks 1 along gas-guide tube 32；It should be noted that gas is from leading in order to prevent
Liquid pipe 31 is discharged, and catheter 31 can be connected to sealing container, or control liquid level by valve and carry out liquid to catheter 31
Envelope.
It is additionally provided between gas-liquid separation unit 3 and burner 1 and provides the first air-introduced machine 4 of oil gas for burner 1,
To provide power along pipe motion to oil gas.
The mixed cell 5 of one Yu air communication are additionally provided between first air-introduced machine 4 and burner 1, the mixing is single
Member 5 inside have netted channel, oil gas moves in mixed cell 5 mixed with air after enter back into burner 1
It is interior.
In order to ensure having enough oxygen in burner 1 and increasing gas flow rate, prevent oil gas from converging, burner 1
Inlet end, that is, gas mixer 12 be also connected with one second air-introduced machine 6, second air-introduced machine 6 is that burner 1 provides sky
Gas.
In order to ensure this system safety, the fire arrester for preventing tempering is additionally provided between mixed cell 5 and burner 1
7, in preferred embodiment, fire arrester 7 is also equipped between the first air-introduced machine 4 and gas-liquid separation unit 3.
Particular embodiments described above has carried out into one the purpose of this utility model, technical scheme and beneficial effects
Step is described in detail, it should be understood that the foregoing is merely specific embodiment of the utility model, are not limited to this reality
With novel, under the premise of not departing from the spirit and principles of the utility model, those of ordinary skill in the art are to the utility model
Any modification, equivalent substitution, improvement and etc. done, should all fall into the utility model claims book determine protection scope it
It is interior.
Claims (10)
1. a kind of oil gas burner, it is characterised in that: including the combustion chamber being arranged along the vertical direction, connect below the combustion chamber
It is connected to a gas mixer, there is a combustion head above combustion chamber, oil gas is mixed with air by gas mixer, mixed gas
It burns in combustion head.
2. a kind of oil gas burner according to claim 1, it is characterised in that: the combustion head is with thickness and to cover
The reticular structure of lid combustion chamber cross section, the combustion head can external circuits entire reticular structure is heated.
3. a kind of oil gas burner according to claim 1, it is characterised in that: between gas mixer and combustion head also
It is provided with gas distributor, through-hole for gas to pass through is evenly equipped on the gas distributor.
4. a kind of oil gas burner according to claim 1, it is characterised in that: be additionally provided with above combustion head to burning
The flue detector that gas componant afterwards is detected.
5. using the oil vapor treatment system of the described in any item oil gas burners of claim 1-4, it is characterised in that: along oil gas
The gas-liquid separation unit that travelling route successively includes the condensing unit condensed to oil gas, is separated to condensed oil gas
With the burner for carrying out burning processing to remaining oil gas.
6. a kind of oil vapor treatment system according to claim 5, it is characterised in that: the gas-liquid separation unit bottom setting
There is catheter, top is provided with the gas-guide tube being connected to adsorption tanks.
7. a kind of oil vapor treatment system according to claim 5, it is characterised in that: gas-liquid separation unit and burner it
Between be additionally provided with and provide the first air-introduced machine of oil gas for burner.
8. a kind of oil vapor treatment system according to claim 7, it is characterised in that: between the first air-introduced machine and burner
It is additionally provided with the mixed cell of one Yu air communication, there is netted channel inside the mixed cell.
9. a kind of oil vapor treatment system according to claim 8, it is characterised in that: the mixed cell and burner it
Between and the first air-introduced machine and gas-liquid separation unit between be respectively arranged with fire arrester.
10. a kind of oil vapor treatment system according to claim 5, it is characterised in that: the inlet end of the burner is also
It connects promising burner and the second air-introduced machine of air is provided.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821685997.9U CN209325791U (en) | 2018-10-17 | 2018-10-17 | A kind of oil gas burner and oil vapor treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821685997.9U CN209325791U (en) | 2018-10-17 | 2018-10-17 | A kind of oil gas burner and oil vapor treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209325791U true CN209325791U (en) | 2019-08-30 |
Family
ID=67708396
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821685997.9U Active CN209325791U (en) | 2018-10-17 | 2018-10-17 | A kind of oil gas burner and oil vapor treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209325791U (en) |
-
2018
- 2018-10-17 CN CN201821685997.9U patent/CN209325791U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201836900U (en) | Internal-combustion biogas incineration torch | |
| CN110440244A (en) | A kind of low concentration gas differential burner | |
| CN107191922A (en) | Low nitrogen burning CFBB | |
| CN201582812U (en) | Pulverized coal burner for oxygen-rich local combustion-supporting | |
| CN209325791U (en) | A kind of oil gas burner and oil vapor treatment system | |
| CN107575856B (en) | A kind of flue gas recirculation boiler system | |
| CN205383616U (en) | Processing system suitable for rich acetylene torch gas | |
| CN105299661B (en) | A kind of processing system and method suitable for rich acetylene torch gas | |
| CN201083388Y (en) | Oily discharge gas backfire-proof combusting device | |
| CN208332302U (en) | A kind of waste-heat recovery device of biomass fuel combustion furnace | |
| CN208222852U (en) | A kind of gas fired-boiler with flue gas heat recovery system | |
| CN106402878B (en) | A kind of incinerator of acid tail gas containing liquid | |
| CN2895751Y (en) | Exhaust-gas temperature-reducing, smoke-eliminating and defoging apparatus fo tunnel diesel-oil generator | |
| CN203484026U (en) | Graded water-seal device for waste gases | |
| CN206496351U (en) | A kind of incinerator of acid tail gas containing liquid | |
| CN202188505U (en) | Regenerative blast-furnace gas diffuse combustor | |
| CN102853535A (en) | Biomass particle hot-water boiler with double combustion chambers | |
| CN209013213U (en) | A kind of closed type high temperature combustion gasses purification device | |
| CN208936178U (en) | A kind of bitumen flue gas processing system of heat recovery | |
| CN104743578B (en) | A kind of well mine salt bittern preprocess method | |
| CN204115495U (en) | A kind of carbonization treatment apparatus | |
| CN209325792U (en) | A kind of oil gas tail gas burner | |
| CN201772468U (en) | Novel incinerator for high-concentration organic toxic waste liquid | |
| CN208620389U (en) | Device is fired in a kind of flue gas multiplexing anaerobism burning and secondary oxygenating again | |
| CN205448279U (en) | Vertical coal fired boiler of burning tied in a bundle |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20201112 Address after: 2803-1, 24th floor, No.1 building, No.12 yard, Zhongguancun South Street, Haidian District, Beijing 100081 Patentee after: ECOTEC ECO-TEC ASIA (BEIJING) Co.,Ltd. Patentee after: JIANGSU AEROSPACE HEWLETT ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Address before: 212200, Jiangsu Zhenjiang Yangzhong industrial storage area along the line 2 Patentee before: JIANGSU AEROSPACE HEWLETT ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. |