CN105042602B - A kind of gas-liquid incinerator - Google Patents
A kind of gas-liquid incinerator Download PDFInfo
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- CN105042602B CN105042602B CN201510486295.2A CN201510486295A CN105042602B CN 105042602 B CN105042602 B CN 105042602B CN 201510486295 A CN201510486295 A CN 201510486295A CN 105042602 B CN105042602 B CN 105042602B
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- 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
- Y02E20/12—Heat utilisation in combustion or incineration of waste
Abstract
The invention discloses a kind of gas-liquid incinerator, including combustible gas combustion control system, gas-liquid mixed combustion control system and liquid combustion control system, first burns furnace tube, second burns furnace tube, 3rd burns furnace tube, premixed opposed firing device, cartridge type gas-liquid premixed swirl burner, spill gas-liquid premix burner, first burning interface channel, second burning interface channel, PLC control cabinet, vapour system, ignition system, instrument air system, nitrogen system and ups power, premixed opposed firing device, cartridge type gas-liquid premixed swirl burner and spill gas-liquid premix burner are separately mounted to the first burning furnace tube, second, which burns furnace tube and the 3rd, burns the inside of furnace tube.Present invention design is reasonable, easy to operate, reduces floor space, and investment reduction, solution take up a large area, invest the defects of big.
Description
Technical field
The present invention relates to flammable gas-liquid incineration technology field, is specifically that one kind automatically controls gas-liquid incinerator.
Background technology
Largely harmful combustible exhaust gas, harmful flammable waste liquid are produced in the refining process such as existing petrochemical industry, coal chemical industry,
Usual gas production body diffuses after carrying out burning processing to exhaust gas with ground torch assembly or overhead torch device；Flammable waste liquid uses
Discharged after the burning of liquid incinerator.Due to distinguishing processing gas and liquid burning processing using two kinds of techniques, cause floor space
Greatly, cost of investment is high, operating cost is high.
The content of the invention
It is above-mentioned to solve it is an object of the invention to provide the gas-liquid incinerator that a kind of floor space is small, operating cost is low
The problem of being proposed in background technology.
To achieve the above object, the present invention provides following technical solution：
A kind of gas-liquid incinerator, including combustible gas interface, low temperature LNG air-liquid pipelines, the first windbreak, the second windbreak,
Third gear brattice, first burn furnace tube, the second burning furnace tube, the 3rd burning furnace tube, premixed opposed firing device, cartridge type
Gas-liquid premixed swirl burner, spill gas-liquid premix burner, the first burning interface channel, the second burning interface channel, PLC controls
Cabinet, vapour system, ignition system, instrument air system, nitrogen system and ups power/generator processed, described first burns furnace tube
Body, the second burning furnace tube and the 3rd burning furnace tube are sequentially arranged at the first windbreak, the second windbreak, the 3rd from front to back
The inside of windbreak, the inside of the first burning furnace tube, the second burning furnace tube and the 3rd burning furnace tube are equipped with pottery
Porcelain fibre module, the premixed opposed firing device are installed on the first inside for burning furnace tube, the combustion of cartridge type gas-liquid premixed swirl
Burner is installed on the second inside for burning furnace tube, and spill gas-liquid premix burner is installed on the 3rd inside for burning furnace tube,
It is described first burning furnace tube in be additionally provided with the first cylinder altar lamp, first burning furnace tube on be also equipped with the first ultraviolet flame
Monitor and the first Infrared video image collection monitor, it is described second burning furnace tube in be additionally provided with the second cylinder altar lamp,
It is also equipped with the second ultraviolet flame monitor and the second Infrared video image collection monitor on second burning furnace tube, described the
Three burning furnace tubes in be additionally provided with the 3rd cylinder altar lamp, the 3rd burning furnace tube on be also equipped with the 3rd ultraviolet flame monitor
Monitor is gathered with the 3rd Infrared video image, the first burning interface channel is installed on the first burning furnace tube and second and burns
Between burning furnace tube, the first burning interface channel liquidates pilot and first passage altar lamp equipped with first passage, and described the
Two burning interface channels are installed on second and burn between furnace tube and the 3rd burning furnace tube, are equipped with the second burning interface channel
Second channel liquidates pilot and second channel altar lamp, passed sequentially through on the left of the combustible gas interface the first liquid separation tank and
Water sealed tank connection classification manifold, classification manifold is equipped with first pressure transmitter, and the classification manifold other ends are connected to
Multiple first order classification branch pipes and multiple second level classification branch pipe, the first order classification branch pipe sequentially pass through the first windbreak and
First burning furnace tube is connected with premixed opposed firing device, and the second level is classified branch pipe and sequentially passes through the second windbreak and the
Two burning furnace tubes are connected with cartridge type gas-liquid premixed swirl burner, on the first order classification branch pipe and second level classification branch pipe
Be designed with the 6th hand-operated valve, turn left on the first order classification branch pipe on the left of the 6th hand-operated valve from the right side be equipped with successively the first spark arrester,
First flowmeter, second pressure transmitter, the second level classification branch pipe on the left of the 6th hand-operated valve are equipped with the first bypass and first
Pneumatic operated valve connects, and the left end of the first pneumatic operated valve is connected with the first pneumatic control valve, and the first left side bypassed is connected with quick-fried for the first time
Fragmentation connects, and the other end of the other end of the first rupture disk and the first pneumatic control valve is classified branch pipe by the second level respectively and connects
Furnace tube and second is burned into first and burns furnace tube, and first flowmeter and second also are provided with the second level classification branch pipe
Pressure transmitter；
The low temperature LNG air-liquid pipelines connect the second liquid separation tank, the second liquid separation tank respectively with the first branch pipe and the second branch pipe
Connection, the first branch pipe are connected with hand-operated valve, the other end and liquid electrodynamic pump, the first bypass hand valve of liquid electrodynamic pump of hand-operated valve
And the second bypass hand valve of liquid electrodynamic pump connects, and liquid level gauge and the 3rd pressure inverting are provided with the second liquid separation tank
Device, the right side is turned left between the liquid electrodynamic pump and liquid manifold is connected with first manual valve, the first check valve, by pipeline
One pressure maintaining valve, second flowmeter and the 4th pressure transmitter, the first automatic voltage regulation circuit and the are equipped with the liquid electrodynamic pump
Two manual loop of voltage regulation；First bypass hand valve one end is connected by pipeline with the first branch pipe, the other end of the first bypass hand valve
It is connected successively with the second check valve, the first return valve and the second manually-operated gate；The bypass of design second on second manual loop of voltage regulation
Hand valve, one end of the second bypass hand valve are connected by pipeline with the first branch pipe, the second bypass hand valve other end by pipeline and
Second manually-operated gate, one end of pressure maintaining valve on main road fluid pipeline are connected；In the connecting pipe of pressure maintaining valve and liquid manifold
Upper setting second flowmeter and the 4th pressure transmitter；The left end of the liquid manifold is connected with multiple 5th branch pipes and multiple
Six branch pipes, the left end of the 5th branch pipe sequentially pass through the second windbreak and second and burn the combustion of furnace tube connecting cylinder formula gas-liquid premixed swirl
Burner, the left end of the 6th branch pipe sequentially pass through third gear brattice and the 3rd and burn furnace tube connection spill gas-liquid premix burner,
5th branch pipe and the 6th branch pipe turn left from the liquid manifold right sides be equipped with the 4th manually-operated gate, the second pneumatic adjusting successively respectively
Valve, the 3rd pneumatic control valve, the 5th manually-operated gate, the 4th flowmeter and the 5th pressure transmitter；
Gas main is equipped with the 6th pressure transmitter, and the left end of gas main is connected with third level classification branch pipe, described
Third level classification branch pipe is equipped with the 7th manually-operated gate, the second spark arrester, and fourth stage classification branch pipe is equipped with the 7th manually-operated gate,
The 7th manually-operated gate other end is connected with the second bypass, operated pneumatic valve, and the other end of operated pneumatic valve is connected with regulating valve；By in the of second
The logical other end is connected with rupture disk；The regulating valve other end, rupture disk be connected respectively with the 4th classification branch pipe into incinerator and
Spill gas-liquid premix burner connects；The 5th flowmeter and the 7th pressure transmitter are set on the 4th classification branch pipe.
As the further scheme of the present invention：The first cylinder altar lamp, the second cylinder altar lamp, the 3rd cylinder are kept burning day and night
Lamp, first passage altar lamp and second channel altar lamp are all connected with ignition system, the first Infrared video image collection monitoring
It is device, the first ultraviolet flame monitor, the second Infrared video image collection monitor, the second ultraviolet flame monitor, the 3rd infrared
Video image acquisition monitor, the 3rd ultraviolet flame monitor and ignition system are all connected with PLC control cabinet.
As the further scheme of the present invention：The first passage liquidates pilot and second channel liquidates pilot
Include burner fuel gas interface, combustion gas left-hand nozzle, combustion gas perpendicular nozzle, combustion gas dextrad nozzle and multiple Gas Pipes, the combustion
Tracheae links burner fuel gas interface, and the combustion gas left-hand nozzle, combustion gas perpendicular nozzle and combustion gas dextrad nozzle are installed in combustion
On tracheae, combustion gas left-hand nozzle vertical left tilts 10-45 °, and combustion gas dextrad nozzle vertical-right tilts 10-45 °.
As the further scheme of the present invention：The premixed opposed firing device includes opposed firing device fuel gas interface, right
Rush burner vapor interface, blower cover, opposed firing device gas inlet, opposed firing device steam pipe branch pipe and opposed firing device
Combustion gas branch pipe, the opposed firing device steam pipe branch pipe connect opposed firing device vapor interface；Opposed firing device combustion gas branch pipe connects
Connect opposed firing device fuel gas interface；The opposed firing device combustion gas branch pipe is installed on the top of steam pipe branch pipe；The combustion that liquidates
Burner gas inlet is connected with opposed firing device combustion gas branch pipe, and the opposed firing device combustion gas branch pipe is equipped with opposed firing device
Gas nozzle, and opposed firing device gas nozzle and opposed firing device gas inlet unicom, the opposed firing device gas injection
The periphery of mouth is exported equipped with the air mixture of opposed firing device, and the opposed firing device steam pipe branch pipe is steamed equipped with opposed firing device
Vapour nozzle.
As the further scheme of the present invention：The cartridge type gas-liquid premixed swirl burner include fluid injector, spinning disk,
Gas nozzle, burner combustion gas branch pipe, steam branch pipe, combustion gas endless tube, steam pipe, Gas Pipe and fluidic interface, the eddy flow combustion
Burner fluid injector connects fluidic interface, and burner cylinder, the spinning disk are equipped with outside the turbulent burner fluid injector
And gas nozzle is installed between turbulent burner fluid injector and burner cylinder, and spinning disk is located at the interior of gas nozzle
Portion；The combustion gas endless tube and steam pipe are installed in fluid injector surrounding, and combustion is connected with the turbulent burner combustion gas endless tube
Burner combustion gas branch pipe, burner combustion gas branch pipe is equipped with multiple gas premixing nozzles, and gas nozzle is arranged on combustion gas branch pipe two
Side；Multiple steam branch pipes are connected with the turbulent burner steam pipe, steam branch pipe is equipped with multiple steam jets, is burning
Windshield is provided with the outside of device；
As the further scheme of the present invention：The spill gas-liquid premix burner include spill burner liquid nozzle,
Spill burner gas nozzle, upper strata deflector, lower floor's deflector, spill burner combustion gas branch pipe, baltimore groove, spill burner
Fuel gas interface, the second vapor interface of the first vapor interface of spill burner, spill burner liquid interface and spill burner, institute
State spill burner combustion gas branch pipe and spill burner fuel gas interface, the spill combustion are connected by spill burner gas connection pipe
Burner gas nozzle is located on spill burner combustion gas branch pipe, and the baltimore groove is installed on the upper of spill burner gas connection pipe
Side, the upper strata deflector and lower floor's deflector are equipped with two, and two upper strata deflectors and Liang Ge lower floors deflector are pacified respectively
Mounted in the both ends of baltimore groove, upper strata deflector is located at the top of lower floor's deflector, and upper strata deflector and the equal position of lower floor's deflector
In the lower section of spill burner gas nozzle, the spill burner liquid nozzle is installed on the centre position of baltimore groove, described
Spill burner mixing nozzle, the spill burner liquid are also equipped with the baltimore groove of spill burner liquid nozzle ends
Nozzle interior is equipped with the second steam jet of spill burner, and spill burner liquid nozzle connects the spill burner liquid and connects
Mouthful, the second steam jet of spill burner connection spill the second vapor interface of burner, the spill burner mixing nozzle
The first steam jet of spill burner is internally provided with, the first steam jet of spill burner connection spill burner first steams
Vapour interface, lower floor's deflector are equipped with flow-guiding mouth, the spill burner mixing nozzle and spill combustion with baltimore groove junction
Liquid inlet is equipped between the first steam jet of burner.
Foregoing invention technology can not compared with prior art, but the beneficial effects of the invention are as follows：
Present invention design is reasonable, easy to operate, and the increase of separate unit burner combustion ability, subtracts in the case of equal discharge capacity
Lack equipment, reduce floor space, investment reduction, solves existing ground gas incinerator and liquid incinerator arrangement and do not conform to
Manage, take up a large area, invest the defects of big.Gas is burned the present invention and liquid burns two kinds of techniques and combines, and utilizes
The advantage such as combustible gas easy firing, easy to control, nominal situation and accident conditions increase the temperature in moment raising stove, after temperature improves,
Do not allow incendive liquid and pernicious gas, be easy to burn at high temperature, while evil gas can decompose completely at high temperature.Subtract
When few separate liquid burns and pernicious gas burns burning is mixed using other fuel；With the saving energy, operating cost, reduce dioxy
Change the technical characterstic such as carbon and oxynitride discharge.
Brief description of the drawings
Fig. 1 is the structure diagram of the present invention.
Fig. 2 is that first passage liquidates pilot in the present invention and second channel liquidates the top view of pilot.
Fig. 3 is that first passage liquidates pilot in the present invention and second channel liquidates the front view of pilot.
Fig. 4 is the top view of premixed opposed firing device in the present invention.
Fig. 5 is the front view of premixed opposed firing device in the present invention.
Fig. 6 is the left view of premixed opposed firing device in the present invention.
Fig. 7 is the front view of opposed firing device gas inlet in the premixed opposed firing device of the present invention.
Fig. 8 is the left view of opposed firing device gas inlet in the premixed opposed firing device of the present invention.
Fig. 9 is the top view of cartridge type gas-liquid premixed swirl burner in the present invention.
Figure 10 is the front view of cartridge type gas-liquid premixed swirl burner in the present invention.
Figure 11 is the top view of middle concave gas-liquid premix burner of the present invention.
Figure 12 is the front view of middle concave gas-liquid premix burner of the present invention.
Embodiment
The technical solution of this patent is described in more detail with reference to embodiment.
- 8 are please referred to Fig.1, a kind of gas-liquid incinerator, including combustible gas interface 1, low temperature LNG air-liquid pipelines 60, first are kept out the wind
Wall 22, the second windbreak 32, third gear brattice 93, first burn furnace tube 18, second and burn the burning furnace tube of furnace tube the 35, the 3rd
Body 95, premixed opposed firing device 16, cartridge type gas-liquid premixed swirl burner 30, spill gas-liquid premix burner 98, first fire
Burn the burning of interface channel 25, second interface channel 36, PLC control cabinet 100, vapour system 101, ignition system 102, instrument air
System 103, nitrogen system 106 and ups power/generator 107, described first, which burns furnace tube 18, second, burns furnace tube 35
The inside of the first windbreak 22,32,93 is sequentially arranged at from front to back with the 3rd burning furnace tube 95, described first burns furnace tube
The inside that body 18, second burns the burning furnace tube 95 of furnace tube 35 and the 3rd is equipped with ceramic fiber module 17, described premixed
Opposed firing device 16, cartridge type gas-liquid premixed swirl burner 30 and spill gas-liquid premix burner 98 are separately mounted to the first burning
Furnace tube 18, second burns the inside that furnace tube 35 and the 3rd burns furnace tube 95；Also set in the first burning furnace tube 18
There is the first cylinder altar lamp 15, the first ultraviolet flame monitor 21 and first is also equipped with the first burning furnace tube 18 and infrared is regarded
Frequency Image Acquisition monitor 20, is additionally provided with the second cylinder altar lamp 31 in the second burning furnace tube 35, second burns furnace tube
Second ultraviolet flame monitor 34 and the second Infrared video image collection monitor 33, the 3rd incinerator are installed on body 35
The 3rd cylinder altar lamp 94 is additionally provided with cylinder 95, the 3rd ultraviolet flame monitor 96 is also equipped with the 3rd burning furnace tube 95
Monitor 97 is gathered with the 3rd Infrared video image, the first burning interface channel 25 is installed on first and burns 18 He of furnace tube
Between second burns furnace tube 35, liquidate pilot 23 and first passage equipped with first passage in the first burning interface channel 25
Altar lamp 24；The second burning interface channel 36 is installed between the second burning burning furnace tube 95 of furnace tube 35 and the 3rd,
Liquidate pilot 38 and second channel altar lamp 37 equipped with second channel in second burning interface channel 36, the combustible gas connects
The left side of mouth 1 passes sequentially through the first liquid separation tank 2 and the connection classification of water sealed tank 3 manifold 5, and classification manifold 5 becomes equipped with first pressure
Device 4 is sent, classification 5 other ends of manifold are connected to multiple first order classification branch pipes 6 and multiple second level classification branch pipe
206, the first order classification branch pipe 6 includes higher level's branch pipe 207 and multiple subordinate's branch pipes 208, and gas classification manifold is total from classification
Pipe separates multiple branch pipes, have spark arrester for the first order, be followed successively by the second level, third level etc. later；It is gradual to be classified diameter branch pipe
Become larger；Liquid is classified manifold, the first order or the second level, the third level etc., and classification diameter branch pipe becomes larger；From classification manifold to
Incinerator is connected to burner, and each pipeline is level-one, the other end of higher level's branch pipe 207 and subordinate's branch pipe 208 it is another
One end sequentially passes through the first windbreak 22 and the first burning furnace tube 18 is connected with premixed opposed firing device 16；Described second
The other end of level classification branch pipe 206 sequentially passes through the second windbreak 32 and second and burns furnace tube 35 and cartridge type gas-liquid premixed swirl
Burner 30 connects；Turn left on higher level's branch pipe 207 from the right side and be equipped with the 6th manually-operated gate 7 and the first spark arrester 8, subordinate successively
Turn left on branch pipe 208 and second level classification branch pipe 206 from the right side and be equipped with the first bypass 9, first flowmeter 13 and second pressure successively
Transmitter 14, turns left from 7 right side of the 6th hand-operated valve and is equipped with the first pneumatic operated valve 10, the first pneumatic control valve 12 successively；It is right from hand-operated valve 7
Turn left while connect the first rupture disk 11, the other end of the other end of the first rupture disk 11 and the first pneumatic control valve 12 passes through
Two level is classified branch pipe 206 and is connected with burning the premixed opposed firing device 16 of stove, the other end of the first rupture disk 11 and the first pneumatic tune
The other end for saving valve 12 is connected by the second classification 206 cartridge type gas-liquid premixed swirl burner 30 of branch pipe；The low temperature LNG gas-liquids
Pipeline 60 connects the second liquid separation tank 61, and the second liquid separation tank 61 is connected respectively by the first branch pipe 62 and the second branch pipe 84 respectively, liquid
Body electrodynamic pump 66 and gas classification manifold 86, are provided with 63 and the 3rd pressure transmitter of liquid level gauge on the second liquid separation tank 61
64, the left end connection liquid manifold 70 of the liquid electrodynamic pump 66, turns left between liquid electrodynamic pump 66 and liquid manifold 76 from the right side
First manual valve 67, the first check valve 68, the first pressure maintaining valve 69,77 and the 4th pressure transmitter of second flowmeter are equipped with successively
76, the right end of the liquid electrodynamic pump 66, which is set, bypasses two-way branch pipe, the first bypass hand valve 71 and manifold hand-operated valves 65 on branch pipe
Connection, 71 other end of the first bypass hand valve are connected with the second check valve 72, the first overflow valve 73, the second manually-operated gate 74 successively,
Manifold hand-operated valves 65 are connected with the second bypass hand valve 75, and 75 other end of the second bypass hand valve, the second manually-operated gate 74 pass through pipeline
It is connected with the other end of the first pressure maintaining valve 69；The left end of the liquid manifold 70 is connected with multiple 5th branch pipes 99 and the multiple 6th
Branch pipe 126, the left end of the 5th branch pipe 99 sequentially passes through the second windbreak 32 and the second burning connection of furnace tube 35 cartridge type gas-liquid is pre-
Mixed turbulent burner 30, the left end of the 6th branch pipe 126 sequentially pass through third gear brattice 93 and the 3rd burn furnace tube 95 connect it is recessed
Shape gas-liquid premix burner 98, the 5th branch pipe 99 and the 6th branch pipe 126 are turned left from the right side is equipped with the 4th manually-operated gate successively
78th, the second pneumatic control valve 79, the 3rd pneumatic control valve 80, the 5th manually-operated gate 81, the 4th flowmeter 82 and the 5th pressure become
Send device 83；The 6th pressure transmitter 85 is additionally provided with the gas main 86, the left end of gas main 86 is connected with the fourth stage point
Level branch pipe 127, the fourth stage classification branch pipe 127 are equipped with the 7th manually-operated gate 87, the second spark arrester 90, the 5th flowmeter 57
With the 7th pressure transmitter 59；Next classification branch pipe 127 is turned left from the right side is equipped with the 7th manually-operated gate 87, the 7th manually-operated gate successively
87 are connected with the second bypass 58, and rupture disk 89, the other end and the fourth stage classification branch pipe of rupture disk 89 are installed in the second bypass 58
127 connections；7th manually-operated gate 87 is connected with operated pneumatic valve 88, regulating valve 91 successively at the same time, the other end of regulating valve 91 and the
Four-stage grading branch pipe 127 connects, and the 5th flowmeter 57, the 7th pressure transmitter 59 are installed on fourth stage classification branch pipeline；
Fourth stage classification branch pipe 127 enters in the 3rd burning furnace tube 95 to be connected with spill gas-liquid premix burner 98.
Fuel gas passes through by combustible gas interface 1, the first liquid separation tank 2, water sealed tank 4 and first order classification branch pipe 6 successively
First spark arrester 8 enters in premixed opposed firing device 16, and the burning things which may cause a fire disaster of the first cylinder altar lamp 15 will premix delta hedge delta combustion
The combustible gas that burner 16 sprays is lighted；When first pressure transmitter 4 detects pressure rise, signal reaches PLC control cabinet
100, PLC control cabinet 100 sends signal and opens the first pneumatic operated valve 10, the first pneumatic control valve 12, and fuel gas enters premix
Burn in delta hedge delta burner 16, when first pressure transmitter 4 continues to detect pressure rise, open the 9, first gas of bypass successively
Dynamic 10 and first pneumatic control valve 12 of valve, fuel gas, which enters in premixed opposed firing device 16, to burn, when detect pressure after
Similarly open every level-one when of continuing rising high successively, the flowmeter 14 set on each stepped pipeline detect flow it is excessive or
Signal is uploaded to PLC control cabinet 100 when too small, and sending instruction the first pneumatic control valve 12 of startup by PLC control cabinet 100 carries out
Adjust flow；When first pressure transmitter 4 detects that pressure reduces, PLC control cabinet 100 sends signal control and closes respectively most
Open startup the first pneumatic operated valve 10 of stepped pipeline afterwards and the first pneumatic control valve 12 is closed successively, when the first pneumatic operated valve 10 and the
When one pneumatic control valve, 12 failure and power failure, fuel gas enters premixed opposed firing by 9 and first rupture disk 11 of bypass
Burn in device 16.
When the first incinerator reaches at full capacity, fuel gas is by being classified branch pipe into the cartridge type gas in the second incinerator
Liquid premixed swirl burner 30 sprays burning, is burned first between furnace tube 18 and second burns furnace tube 35 and is equipped with the first combustion
Interface channel 25 is burnt, fuel gas liquidates pilot 23 by first passage and first passage altar lamp 24 lights burning, institute
State first passage liquidate pilot 23 and first passage altar lamp 24 by the control of PLC control cabinet 100 carry out it is automatic light and
Close；Other discharge burners at different levels are mutually ignited by altar lamp or burner.
LNG cryogenic liquids or other gas-liquid mixtures fill 62 and gas main by low temperature LNG air-liquid pipelines 61, the second liquid separation
83 enter in the 3rd spill gas-liquid premix burner 92 for burning furnace tube 41；Spill gas-liquid premix burner 92 sprays combustible gas
Body, is led to by burning the second of the second burning interface channel 23 set between the burning furnace tube 41 of furnace tube 40 and the 3rd second
Road liquidates pilot 30 and second channel altar lamp 24 lights burning, 20 and second interface channel 23 of the first interface channel
Formed by steel plate and heat-barrier material, the 97 equal heatproof of heat-barrier material and ceramic fiber module is more than 1200 DEG C, described second
Liquidate pilot 30 and second channel altar lamp 24 of passage is lighted and closes it automatically by the control of PLC control cabinet 100
Its discharge burner at different levels is mutually ignited by altar lamp or burner；
When liquid level gauge 63 detects that the liquid level of the second liquid separation tank 61 exceedes setting value, PLC control cabinet 100 sends instruction and opens
Hydrodynamic body electrodynamic pump 66；Liquid manually valve 65, by liquid electrodynamic pump 66, first manual valve 67, the first check valve 68,
First pressure maintaining valve 69, liquid manifold 70, the 4th manually-operated gate 78, the second pneumatic control valve 79 and the 3rd pneumatic control valve 80 enter
3rd burns in furnace tube 95, and is sprayed by spill gas-liquid premix burner 98, since liquid electrodynamic pump 66 is improved in pipeline
Pressure, liquid sprays is atomized after-combustion after spill gas-liquid premix burner 98 by the principle of mechanical atomization；When liquid level gauge 63 after
When the continuous liquid level for detecting the second liquid separation tank 61 raises, 100 output control signal of PLC control cabinet, it is pneumatic to open next stage second
79 and the 3rd pneumatic control valve 80 of regulating valve enters the 3rd spill gas-liquid premix burner 98 burned in furnace tube 95 and sprays combustion
Burn, it is other once to be opened with principle per level-one, when liquid level gauge 63 detects that the liquid level of the second liquid separation tank 61 reduces, automatically step by step
Close per level-one；The second burning furnace tube 40 is entered back into when the 3rd burning furnace tube 41 reaches and meets load to burn, when the 3rd
Pressure transmitter 64 detects when being reduced less than design pressure that PLC control cabinet 100 controls closing liquid electrodynamic pump 66 and classification gas
Dynamic valve 79.
The first cylinder altar lamp 15, the second cylinder altar lamp 31, the 3rd cylinder altar lamp 94, first passage altar lamp
24 and second channel altar lamp 37 be all connected with ignition system 102, PLC control cabinet 100 according to the first ultraviolet flame monitor 20,
The monitoring situation of second ultraviolet flame monitor 33 and the 3rd ultraviolet flame monitor 97 adjusting quantity of steam etc., described first
Infrared video image collection monitor 20, the second Infrared video image collection monitor 34, the 3rd Infrared video image collection prison
Visual organ 96 and ignition system 102 are all connected with PLC control cabinet 100, and the parameters such as quantity of steam are adjusted according to monitoring flame incineration situation；When
First cylinder Infrared video image collection monitor 26, the second cylinder Infrared video image collection 28 and the 3rd cylinder of monitor are red
When outer video image acquisition monitor detects fuel gas and liquid burning over-emitting black exhaust, then PLC control cabinet 100, which automatically turns on, steams
Steam valve door, steam bring substantial amounts of air into, and steam and air spray burner, the steam and air of eddy flow shape in rotary manner
Mixed gas is mixed with combustion gas and fog-like liquid, the burning of burning mixture moment；PLC control cabinet 100 according to fuel gas and
How much control ignition systems 102 of the amount of LNG cryogenic liquids carry out automatic ignition or closing.
Described first shape for burning the burning burning furnace tube 95 of furnace tube 35 and the 3rd of furnace tube 18, second is polygon water chestnut
Shape, square, rectangle, circle or other shapes.
The first passage liquidates pilot 23 and second channel liquidates, and pilot 38 includes burner fuel gas interface
205th, combustion gas left-hand nozzle 202, combustion gas perpendicular nozzle 203, combustion gas dextrad nozzle 204 and multiple Gas Pipes 201, the Gas Pipe
201 link burner fuel gas interface 205, the combustion gas left-hand nozzle 202, combustion gas perpendicular nozzle 203 and combustion gas dextrad nozzle 204
It is installed in Gas Pipe 201.
The premixed opposed firing device 16 includes opposed firing device fuel gas interface 310, opposed firing device vapor interface
312nd, blower cover 316, opposed firing device gas inlet 301, opposed firing device steam pipe branch pipe 302 and opposed firing device combustion gas
Branch pipe 303, the opposed firing device steam pipe branch pipe 302 connect opposed firing device vapor interface 312, opposed firing device combustion gas branch
Pipe 303 connects opposed firing device fuel gas interface 310, and the opposed firing device combustion gas branch pipe 303 is installed on pair by blower cover 316
The top of burner steam pipe branch pipe 302 is rushed, the opposed firing device gas inlet 301 connects opposed firing device combustion gas branch pipe
303, opposed firing device gas nozzle 305, and opposed firing device combustion gas are also provided with the opposed firing device combustion gas branch pipe 303
Nozzle 305 and 301 unicom of opposed firing device gas inlet, the periphery of the opposed firing device gas nozzle 305, which is equipped with, to liquidate
Burner air mixture outlet 306, the opposed firing device steam pipe branch pipe 302 is equipped with opposed firing device steam jet 304.
The premixed opposed firing device 16 is pre-mixing type combustion apapratus, and nozzle is nozzle self-suction type combustor, premixed opposed firing device
16 can be designed as the shapes such as T circumferentials, T rectangles.
The cartridge type gas-liquid premixed swirl burner 21 includes turbulent burner fluid injector 801, spinning disk 802, eddy flow
Burner gas nozzle 803, blower cover 818, burner combustion gas branch pipe 805, turbulent burner steam branch pipe 807, swirl flow combustion
Device combustion gas endless tube 808, turbulent burner steam pipe 809, turbulent burner Gas Pipe 810 and turbulent burner fluidic interface 816,
The turbulent burner fluid injector 801 connects turbulent burner fluidic interface 816, the turbulent burner fluid injector 801
Outside is equipped with burner cylinder 811, and the spinning disk 802 and turbulent burner gas nozzle 803 are installed in turbulent burner
Between fluid injector 801 and burner cylinder 811, and spinning disk 802 is located at the inside of turbulent burner gas nozzle 803, institute
State turbulent burner combustion gas endless tube 808 and turbulent burner steam pipe 809 be installed on turbulent burner fluid injector 801,
Burner combustion gas branch pipe 805 is connected with the turbulent burner combustion gas endless tube 808, burner combustion gas branch pipe 805 is equipped with rotation
Burner gas premixing nozzle 804 is flowed, turbulent burner steam branch pipe 807 is connected with the turbulent burner steam pipe 809,
Turbulent burner steam branch pipe 807 is equipped with turbulent burner steam jet 806, and the level angle of the spinning disk 802 is 0-
45°。
The spill gas-liquid premix burner 98 includes spill burner liquid nozzle 501, spill burner gas nozzle
502nd, upper strata deflector 503, lower floor's deflector 504, spill burner combustion gas branch pipe 505, baltimore groove 508, the combustion of spill burner
Gas interface 509, the second steam of the first vapor interface of spill burner 510, spill burner liquid interface 511 and spill burner
Interface 517, the spill burner combustion gas branch pipe 505 connect spill burner by spill burner gas connection pipe 507 and fire
Gas interface 509, the spill burner gas nozzle 502 are located on spill burner combustion gas branch pipe 505, the baltimore groove 508
Installed in the top of spill burner gas connection pipe 507, the upper strata deflector 503 and lower floor's deflector 504 are equipped with two
A, two upper strata deflectors 503 and Liang Ge lower floors deflector 504 are separately mounted to the both ends of baltimore groove 508, upper strata deflector
503 are located at the top of lower floor's deflector 504, and upper strata deflector 503 and lower floor's deflector 504 are respectively positioned on spill burner gas
The lower section of nozzle 502,504 interlaced arrangement of upper strata deflector 503 and lower floor's deflector, the spill burner liquid nozzle 501
Installed in the centre position of baltimore groove 508, the angle that spill burner liquid nozzle 501 sprays liquid is horizontal 10-120 °, institute
State and spill burner mixing nozzle 506 is also equipped with the baltimore groove 508 at 501 both ends of spill burner liquid nozzle, it is described recessed
Shape burner liquid nozzle 501 is internally provided with the second steam jet of spill burner 518, and spill burner liquid nozzle 501 connects
The spill burner liquid interface 511 is connect, the second steam jet of spill burner 518 connects spill the second steam of burner and connects
Mouth 517, the spill burner mixing nozzle 506 are internally provided with the first steam jet of spill burner 516, the spill combustion
The first steam jet of burner 516 connects the first vapor interface of spill burner 510, lower floor's deflector 504 and baltimore groove 508
Junction is equipped with flow-guiding mouth 512, between the spill burner mixing nozzle 506 and the first steam jet of spill burner 516
Equipped with liquid inlet 513, first steam jet of spill burner 516 is steam ejection nozzle, by steam ejection by liquid
Body, which sprays, carries out spray burning.The liquid mixes ejection atomization by steam or compressed air.
When using spill gas-liquid premix burner 92, spill burner liquid nozzle 501 is arranged on spill gas-liquid premix
The centre of burner 92, two layers of deflector, the spray of upper strata deflector fixed concave burner gas are set in gas burner below
Mouth 502, design and 502 equidirectional oblong aperture of spill burner gas nozzle or other shapes in the fixed plate of upper strata deflector
The hole of shape；The fixed plate surrounding of lower floor's deflector is high, 92 center of both sides slope aspect spill gas-liquid premix burner, when liquid exceedes spray
During mouth air inlet, steam suction sprays burning, and the cryogenic mechanical atomized liquid that nozzle sprays is mixed with steam, and moment improves mixing
Gas temperature burns, and is filled in the second liquid separation and liquid level gauge 63 is provided with 62, and liquid level gauge 63 detects liquid in the second liquid separation filling 62
Rise, controls start liquid electrodynamic pump 66, liquid is fired by pipeline into cartridge type gas-liquid premixed swirl by PLC control cabinet 100
Burn in burner 30 or spill gas-liquid premix burner 98；Liquid level reduces or the in liquid level gauge 63 detects that the second liquid separation fills 61
When being negative pressure in two liquid separations filling 61, close valve and stop liquid electrodynamic pump 66, liquid control system are controlled by PLC control cabinet 100
Stop is only burnt, and system enters monitored state.
Liquid combustion control system does not control with gas-liquid burner, liquid combustion control system can have a set of incinerator or
Combustion System, liquid combustion system are suitable for LNG cryogenic liquids and other low temperature, high-temp liquid to more than two sets of incinerator at the same time
Control is burned, and gas incineration system is burnt into incinerator at the same time with liquid incineration system, and burner independent control, fires at the same time
Burn.
Present invention design is reasonable, easy to operate, and the increase of separate unit burner combustion ability, subtracts in the case of equal discharge capacity
Lack equipment, reduce floor space, investment reduction, solves existing ground gas incinerator and liquid incinerator arrangement and do not conform to
Manage, take up a large area, invest the defects of big.Gas is burned the present invention and liquid burns two kinds of techniques and combines, and utilizes
The advantage such as combustible gas easy firing, easy to control, nominal situation and accident conditions increase the temperature in moment raising stove, after temperature improves,
Do not allow incendive liquid and pernicious gas, be easy to burn at high temperature, while evil gas can decompose completely at high temperature.Subtract
When few separate liquid burns and pernicious gas burns burning is mixed using other fuel；With the saving energy, operating cost, reduce dioxy
Change the technical characterstic such as carbon and oxynitride discharge.
The better embodiment of this patent is explained in detail above, but this patent is not limited to above-mentioned embodiment party
Formula, can also be on the premise of this patent objective not be departed from the knowledge that one skilled in the relevant art possesses
Various changes can be made.
Claims (5)
1. a kind of gas-liquid incinerator, including combustible gas interface (1), low temperature LNG air-liquid pipelines (60), the first windbreak (22),
Two windbreaks (32), third gear brattice (93), first burn furnace tube (18), the second burning furnace tube (35), the 3rd incinerator
Cylinder (95), premixed opposed firing device (16), cartridge type gas-liquid premixed swirl burner (30), spill gas-liquid premix burner
(98), first burning interface channel (25), second burning interface channel (36), PLC control cabinet (100), vapour system (101),
Ignition system (102), instrument air system (103), nitrogen system (106) and ups power/generator (107), its feature exist
In, it is described first burn furnace tube (18), second burn furnace tube (35) and the 3rd burning furnace tube (95) from front to back successively
Installed in the first windbreak (22), the second windbreak (32), third gear brattice (93) inside, it is described first burn furnace tube
(18), the inside of the second burning furnace tube (35) and the 3rd burning furnace tube (95) is equipped with ceramic fiber module (17), described
Premixed opposed firing device (16) is installed on the first inside for burning furnace tube (18), cartridge type gas-liquid premixed swirl burner (30)
The inside for burning furnace tube (35) installed in second, spill gas-liquid premix burner (98) are installed on the 3rd and burn furnace tube (95)
Inside, be additionally provided with the first cylinder altar lamp (15) in first burning furnace tube (18), first burns on furnace tube (18)
It is also equipped with the first ultraviolet flame monitor (21) and the first Infrared video image collection monitor (20), second incinerator
The second cylinder altar lamp (31) is additionally provided with cylinder (35), the second ultraviolet flame prison is also equipped with the second burning furnace tube (35)
Visual organ (34) and the second Infrared video image gather monitor (33), and the 3rd is additionally provided with the 3rd burning furnace tube (95)
Body altar lamp (94), is also equipped with the 3rd ultraviolet flame monitor (96) and the 3rd infrared video in the 3rd burning furnace tube (95)
Image Acquisition monitor (97), the first burning interface channel (25) are installed on first and burn furnace tube (18) and the second burning
Between furnace tube (35), first burning interface channel (25) equipped with first passage liquidate pilot (23) and first passage it is kept burning day and night
Lamp (24), it is described second burning interface channel (36) be installed on second burn furnace tube (35) and the 3rd burning furnace tube (95) it
Between, liquidate pilot (38) and second channel altar lamp (37) equipped with second channel in the second burning interface channel (36), institute
State and the first liquid separation tank (2) and water sealed tank (3) connection classification manifold (5) are passed sequentially through on the left of combustible gas interface (1), be classified manifold
(5) first pressure transmitter (4) is equipped with, classification manifold (5) other end is connected to multiple first order classification branch pipes
(6) and multiple second level classification branch pipe (206), first order classification branch pipe (6) sequentially passes through the first windbreak (22) and the
One burning furnace tube (18) is connected with premixed opposed firing device (16), and the second level is classified branch pipe (206) and sequentially passes through the
Two windbreaks (32) and the second burning furnace tube (35) are connected with cartridge type gas-liquid premixed swirl burner (30), first fraction
Level branch pipe (6) and the second level, which are classified on branch pipe (206), is designed with the 6th hand-operated valve (7), the first order on the left of the 6th hand-operated valve (7)
Turn left on classification branch pipe (6) from the right side and be equipped with the first spark arrester (8), first flowmeter (13), second pressure transmitter (14) successively,
Second level classification branch pipe (206) on the left of 6th hand-operated valve (7) is equipped with the first bypass (9) and the first pneumatic operated valve (10) connection,
The left end of first pneumatic operated valve (10) is connected with the first pneumatic control valve (12), is connected with the left of the first bypass (9) quick-fried for the first time
Fragmentation (11) connects, and the other end of the first rupture disk (11) and the other end of the first pneumatic control valve (12) pass through the second level respectively
It is classified branch pipe (206) connection and enters the first burning furnace tube (18) and the second burning furnace tube (35), the second level classification branch
First flowmeter (13) and second pressure transmitter (14) also are provided with pipe (206)；
The low temperature LNG air-liquid pipelines (60) connect the second liquid separation tank (61), the second liquid separation tank (61) respectively with the first branch pipe
(62) it is connected with the second branch pipe (84) connection, the first branch pipe (62) with hand-operated valve (65), the other end and liquid of hand-operated valve (65)
Second bypass hand valve of electrodynamic pump (66), the first bypass hand valve (71) of liquid electrodynamic pump (66) and liquid electrodynamic pump (66)
(75) connect, liquid level gauge (63) and the 3rd pressure transmitter (64), the liquid electric are installed on the second liquid separation tank (61)
The right side is turned left between dynamic pump (66) and liquid manifold (70) is connected with first manual valve (67), the first check valve by pipeline
(68), the first pressure maintaining valve (69), second flowmeter (77) and the 4th pressure transmitter (76), set in the liquid electrodynamic pump (66)
There are the first automatic voltage regulation circuit and the second manual loop of voltage regulation；First bypass hand valve (71) one end passes through pipeline and the first branch pipe
(62) be connected, first bypass hand valve (71) the other end successively with the second check valve (72), the first return valve (73) and second
Manually-operated gate (74) connects；The bypass hand valve of design second (75) on second manual loop of voltage regulation, the one of the second bypass hand valve (75)
End is connected by pipeline with the first branch pipe (62), and second bypass hand valve (75) other end passes through pipeline and the second manually-operated gate
(74), one end of the first pressure maintaining valve (69) on main road fluid pipeline is connected；It is total in first pressure maintaining valve (69) and liquid
Manage and second flowmeter (77) and the 4th pressure transmitter (76) are set in the connecting pipe of (70)；A left side for the liquid manifold (70)
End is connected with multiple 5th branch pipes (99) and multiple 6th branch pipes (126), and the left end of the 5th branch pipe (99) sequentially passes through second gear
Brattice (32) and second burns furnace tube (35) connection cartridge type gas-liquid premixed swirl burner (30), a left side for the 6th branch pipe (126)
End sequentially passes through third gear brattice (93) and the 3rd and burns furnace tube (95) and connect spill gas-liquid premix burner (98), and described the
Five branch pipes (99) and the 6th branch pipe (126) turn left respectively from liquid manifold (70) right side be equipped with successively the 4th manually-operated gate (78),
Second pneumatic control valve (79), the 3rd pneumatic control valve (80), the 5th manually-operated gate (81), the 4th flowmeter (82) and the 5th pressure
Power transmitter (83)；
Gas main (86) is equipped with the 6th pressure transmitter (85), and the left end of gas main (86) is connected with third level classification branch
Manage (92), the third level classification branch pipe (92) is equipped with the 7th manually-operated gate (87), the second spark arrester (90), fourth stage classification
Branch pipe (127) is equipped with the 7th manually-operated gate (87), the 7th manually-operated gate (87) other end and the second bypass (58), operated pneumatic valve
(88) connect, the other end of operated pneumatic valve (88) is connected with regulating valve (91)；The other end and rupture disk of second bypass (58)
(89) connect；Regulating valve (91) other end, rupture disk (89) be connected respectively with fourth stage classification branch pipe (127) into incinerator and
Spill gas-liquid premix burner (98) connects；5th flowmeter (57) and the 7th pressure are set on fourth stage classification branch pipe (127)
Power transmitter (59)；
The first passage liquidate pilot (23) and first passage altar lamp (24) by PLC control cabinet (100) control into
Row is lighted and closed automatically, and the second channel liquidates pilot (38) and second channel altar lamp (37) is controlled by PLC
Cabinet (100) control is lighted and closed automatically；
The first passage liquidates pilot (23) and second channel liquidates, and pilot (38) includes burner fuel gas interface
(205), combustion gas left-hand nozzle (202), combustion gas perpendicular nozzle (203), combustion gas dextrad nozzle (204) and multiple Gas Pipes (201),
The Gas Pipe (201) is all connected with burner fuel gas interface (205), the combustion gas left-hand nozzle (202), combustion gas perpendicular nozzle
(203) it is installed in combustion gas dextrad nozzle (204) in Gas Pipe (201), combustion gas left-hand nozzle (202) vertical left tilts
10-45 °, combustion gas dextrad nozzle (204) vertical-right tilts 10-45 °.
2. gas-liquid incinerator according to claim 1, it is characterised in that the first cylinder altar lamp (15), second
Body altar lamp (31), the 3rd cylinder altar lamp (94), first passage altar lamp (24) and second channel altar lamp (37) are all connected with
Ignition system (102), the first Infrared video image collection monitor (20), the first ultraviolet flame monitor (21), second
Infrared video image collection monitor (33), the second ultraviolet flame monitor (34), the 3rd Infrared video image collection monitor
(97), the 3rd ultraviolet flame monitor (96) and ignition system (102) are all connected with PLC control cabinet (100).
3. gas-liquid incinerator according to claim 1, it is characterised in that the premixed opposed firing device (16) include pair
Rush burner fuel gas interface (310), opposed firing device vapor interface (312), blower cover (316), opposed firing device gas inlet
Mouth (301), opposed firing device steam pipe branch pipe (302) and opposed firing device combustion gas branch pipe (303), the opposed firing device steam
Pipe branch pipe (302) connection opposed firing device vapor interface (312)；Opposed firing device combustion gas branch pipe (303) connects opposed firing device
Fuel gas interface (310)；The opposed firing device combustion gas branch pipe (303) is installed on the top of steam pipe branch pipe (302)；It is described to liquidate
Burner gas inlet (301) is connected with opposed firing device combustion gas branch pipe (303), the opposed firing device combustion gas branch pipe
(303) opposed firing device gas nozzle (305), and opposed firing device gas nozzle (305) and opposed firing device combustion gas are equipped with
Air inlet (301) unicom, the periphery of the opposed firing device gas nozzle (305) are exported equipped with the air mixture of opposed firing device
(306), the opposed firing device steam pipe branch pipe (302) is equipped with opposed firing device steam jet (304).
4. gas-liquid incinerator according to claim 1, it is characterised in that the cartridge type gas-liquid premixed swirl burner (30)
Including fluid injector (801), spinning disk (802), gas nozzle (803), burner combustion gas branch pipe (805), steam branch pipe
(807), combustion gas endless tube (808), steam pipe (809), Gas Pipe (810) and fluidic interface (816), the turbulent burner liquid
Nozzle (801) connection fluidic interface (816), the turbulent burner fluid injector (801) is exterior to be equipped with burner cylinder
(811), the spinning disk (802) and gas nozzle (803) are installed in turbulent burner fluid injector (801) and burner tube
Between body (811), and spinning disk (802) is located at the inside of gas nozzle (803)；The combustion gas endless tube (808) and steam pipe
(809) fluid injector (801) surrounding is installed in, burner combustion gas is connected with the turbulent burner combustion gas endless tube (808)
Branch pipe (805), burner combustion gas branch pipe (805) is equipped with multiple gas premixing nozzles (804), and gas nozzle (804) is set
In combustion gas branch pipe (805) both sides；Multiple steam branch pipes (807), steam branch are connected with the turbulent burner steam pipe (809)
Pipe (807) is equipped with multiple steam jets (806), and windshield (868) is provided with the outside of burner.
5. gas-liquid incinerator according to claim 1, it is characterised in that the spill gas-liquid premix burner (98) includes
Spill burner liquid nozzle (501), spill burner gas nozzle (502), upper strata deflector (503), lower floor's deflector
(504), spill burner combustion gas branch pipe (505), baltimore groove (508), spill burner fuel gas interface (509), spill burner
First vapor interface (510), spill burner liquid interface (511) and the second vapor interface of spill burner (517), it is described recessed
Shape burner combustion gas branch pipe (505) connects spill burner fuel gas interface by spill burner gas connection pipe (507)
(509), the spill burner gas nozzle (502) is located on spill burner combustion gas branch pipe (505), the baltimore groove
(508) top of spill burner gas connection pipe (507), the upper strata deflector (503) and lower floor's deflector are installed on
(504) two are equipped with, two upper strata deflectors (503) and Liang Ge lower floors deflector (504) are separately mounted to baltimore groove (508)
Both ends, upper strata deflector (503) is located at the top of lower floor's deflector (504), and upper strata deflector (503) and lower floor's deflector
(504) lower section of spill burner gas nozzle (502) is respectively positioned on, the spill burner liquid nozzle (501) is installed on recessed
The centre position of shape groove (508), is also equipped with the baltimore groove (508) at spill burner liquid nozzle (501) both ends recessed
Shape burner mixing nozzle (506), the spill burner liquid nozzle (501) are internally provided with the spray of the second steam of spill burner
Mouth (518), spill burner liquid nozzle (501) connect the spill burner liquid interface (511), spill burner second
Steam jet (518) connection spill the second vapor interface of burner (517), the spill burner mixing nozzle (506) it is interior
Portion is equipped with the first steam jet of spill burner (516), the first steam jet of spill burner (516) connection spill burning
The first vapor interface of device (510), lower floor's deflector (504) are equipped with flow-guiding mouth (512), institute with baltimore groove (508) junction
State and be equipped with liquid inlet (513) between spill burner mixing nozzle (506) and the first steam jet of spill burner (516).
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| CN201510486295.2A CN105042602B (en) | 2015-08-10 | 2015-08-10 | A kind of gas-liquid incinerator |
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| CN107543176A (en) * | 2016-06-27 | 2018-01-05 | 斯文杰 | A kind of mobile vehicle-mounted gas-liquid incinerator |
| CN109659043B (en) * | 2017-10-10 | 2023-10-03 | 中国船舶重工集团公司第七一九研究所 | Ocean nuclear power's suppression test platform |
| CN110207117A (en) * | 2019-06-04 | 2019-09-06 | 岳阳钟鼎热工电磁科技有限公司 | Multi-functional low NOxSelf-priming integration altar lamp |
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| CN205227343U (en) * | 2015-08-10 | 2016-05-11 | 斯文杰 | Burning furnace is burnt to gas -liquid |
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| JPS6123041U (en) * | 1984-07-16 | 1986-02-10 | 株式会社ノーリツ | Forced draft combustion equipment |
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|---|---|---|---|---|
| AU6270173A (en) * | 1972-11-15 | 1975-05-22 | Inst Mosvodokanalniiproekt | Device for burning liquid combustible waster |
| CN2092678U (en) * | 1991-01-29 | 1992-01-08 | 余志平 | Stove burning liquid fuel or gas fuel |
| CN101283161A (en) * | 2005-03-01 | 2008-10-08 | 朱比特氧气公司 | Module-based oxy-fuel boiler |
| CN203571764U (en) * | 2013-11-01 | 2014-04-30 | 吴晓阳 | Ground waste gas burning torch device |
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