CN105642195B - A kind of liquid light hydrocarbon gasification installation - Google Patents
A kind of liquid light hydrocarbon gasification installation Download PDFInfo
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- CN105642195B CN105642195B CN201610130778.3A CN201610130778A CN105642195B CN 105642195 B CN105642195 B CN 105642195B CN 201610130778 A CN201610130778 A CN 201610130778A CN 105642195 B CN105642195 B CN 105642195B
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- hot blast
- light hydrocarbon
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J7/00—Apparatus for generating gases
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/04—Gasification
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Feeding And Controlling Fuel (AREA)
Abstract
, can be by C the invention discloses a kind of liquid light hydrocarbon gasification installation5~C6Fuel gas is turned to Deng light hydrocarbon light petroleum gas, is industrial and civilian offer new cleaning fuel.The liquid light hydrocarbon gasification installation, mainly it is made up of gasification pot, oil plant variable pump, hot blast variable pump and programmable controller.The gasification pot is provided with oil feeding device, air-intake device, safety valve, pressure sensor, thermocouple, gas outlet valve interface, blowoff valve interface and cylinder footing and ground connection；There are hot blast buffering pressure stabilizing chamber, Cyclonic gasifying road, mixed empty room, oily foam separator, air storage chamber and anti-static mesh in the gasification pot.Oil plant variable pump that oil plant and hot blast are automatically controlled by controller, hot blast variable pump are quantitative, constant temperature, fixed than supply, by gasification pot gasification to mix empty fuel gas.The present invention can make the diminution of aerogenesis equipment volume, cost reduction, output increased, steady quality, energy-saving and environment-friendly.
Description
Technical field
The present invention relates to a kind of gasification installation that liquid light hydrocarbon is changed into fuel gas.
Background technology
Liquid light hydrocarbon gasification installation is light hydrocarbon light oil gasifying, while is mixed by a certain percentage with air, is formed mixed
Close the device of gas.For the light hydrocarbon light oil of gas processed, mainly C5（Light dydrocarbon）、C6（Carbon six）And C7（Carbon seven）Deng.At present,
Can be by C5（Light dydrocarbon）It is changed into gaseous state from liquid, and fuel gas is mixed to form with air, it is for people to use.But existing gas
Makeup, which is put, has the drawbacks such as security is poor, the efficiency of heating surface is low, equipment volume is big, gas production is small and produced combustion gas quality is unstable.
Existing one kind《Liquid C 5 vaporisation apparatus》（The patent No.：ZL200720037587.9）, use " still daily seen
The heating element heater of immersion heater, insulating pot ", this heating element heater is inserted into after being powered in the chamber equipped with oil plant and added to oil plant
Heat.So heat, be absolutely unsafe, it may occur that major accident.In routine use, even if heating element heater is placed in jacket pipe,
It is difficult to prevent potential safety hazard, and substantially reduces the efficiency of heating surface.
Now separately there is one kind《Liquid C 5 vaporisation apparatus》（Patent of invention number：ZL2009 10182911.X；Utility model is special
Sharp Authorization Notice No.：CN 201502867U）, using one group of heating element heater to heating medium（Water）Heating, and pass through medium（Water）
Oil plant in tank is conducted heat across tank skin.Its heating high energy consumption, efficiency are low, and device structure is complicated, volume is big, gas production is small.
Now there is one kind《High energy mixes empty light hydrogen cracking kettle》（Number of patent application：201510538133.9）, using PLC intelligence
Control, light hydrocarbon light oil is heated into Bubbler vaporizer, while fuel gas is mixed to form with air.But also fail to solve heating effect
The problems such as rate is low, equipment volume is big, gas production is small and combustion gas quality is unstable.Its control system does not have oil plant and air
Mixing match includes control range, fails to realize optimal, effective, control at any time to oil plant and air stoichiometry.
Three of the above prior art, all it is to utilize C5（Light dydrocarbon）The characteristic of low boiling point is heated Bubbler vaporizer, with air
It is mixed to form lighter hydrocarbons and mixes air gas.But in lighter hydrocarbons mix air gas, light hydrocarbon light oil proportion deficiency one thousandth, other
All it is air, therefore, can be only dropped to oil plant heating it is difficult to ensure that normal gas producing, especially in the winter time, a large amount of cold airs are mixed into
Low heating effect, the gasification for suppressing oil plant, it produces the quality of combustion gas and is difficult to stabilization.Also, because heating effect is poor, gas processed is former
Material is confined to the relatively low C of boiling point5, can not be by C6、C7Combustion gas is turned to Deng light petroleum gas.In addition, existing production lighter hydrocarbons mix air gas
Technology, all fail the effectively mixing match of control oil plant and air, fail to realize the weight feed of oil plant, energy-saving effect is not good enough.
The content of the invention
The present invention solves the technical problem of a kind of liquid light hydrocarbon gasification installation is provided, cost and aerogenesis can be reduced
Cost, energy consumption is saved, production safety, stable aerogenesis quality is ensured, improves gas production, natural air-liquid can be substituted by producing combustion gas
Change gas and coal, be industrial and civilian offer heat energy, it is energy-saving and environment-friendly.
In order to solve the above technical problems, one aspect of the present invention is：
A kind of liquid light hydrocarbon gasification installation, including gasification pot, oil plant variable pump, hot blast variable pump and PLC technology are provided
Device, the top of the gasification pot outer barrel are provided with gas outlet valve interface, safety valve, thermocouple and pressure sensor, the gas
The middle and lower part for changing cylinder outer barrel is equipped with oil feeding device and air-intake device, and the bottom of the gasification pot is provided with blowoff valve interface, cylinder
Footing and ground connection；The chamber of lower section buffers pressure stabilizing chamber, the top dress of the hot blast buffering pressure stabilizing chamber for hot blast in the gasification pot
There is Cyclonic gasifying road, the entrance in the Cyclonic gasifying road communicates with hot blast buffering pressure stabilizing chamber, and is provided with oil inlet pipe and oil plant spray
Mouth is drenched, the outlet in the Cyclonic gasifying road communicates with mixed empty room；The mixed empty room top is oily foam separator and Oil-gas Separation
The top of gas and oil separating plant described in device is air storage chamber, and anti-static mesh is provided with the air storage chamber.
In a preferred embodiment of the present invention, the oil feeding device includes the first check valve, oil-feed interface tube, oil inlet pipe
With oil plant mouth spray, described oil inlet pipe one end is stretched into the Cyclonic gasifying road in the gasification pot by oil-feed interface tube, stretched into
Some oil plant mouth sprays, the other end of the oil inlet pipe are evenly distributed with the oil-feed tube wall in the Cyclonic gasifying road
Connect with the first check valve, first check valve is connected with oil plant variable pump, the oil plant variable pump and programmable controller
It is electrically connected with.
In a preferred embodiment of the present invention, the diameter of the oil plant mouth spray is not more than 1.5mm, some sprays
Mouth sectional area sum is not more than the sectional area of the oil inlet pipe.
In a preferred embodiment of the present invention, the air-intake device includes the second check valve and air inlet valve interface, described
Air inlet valve interface the hot blast buffering pressure stabilizing chamber connected in gasification pot of one end, the other end connects with the second check valve, described the
The other end of two check valves is connected with hot blast variable pump, and the hot blast variable pump is electrically connected with programmable controller.
In a preferred embodiment of the present invention, the bore phase of the bore of the air inlet valve interface and gas outlet valve interface
Deng.
In a preferred embodiment of the present invention, the air storage chamber that the probe of the pressure sensor is stretched into the gasification pot
In, and the pressure information in the air storage chamber is transferred to the programmable controller by being electrically connected with.
In a preferred embodiment of the present invention, the probe of the thermocouple is stretched into the air storage chamber in the gasification pot,
And the temperature information in the air storage chamber is transferred to the programmable controller by being electrically connected with.
In a preferred embodiment of the present invention, the Cyclonic gasifying road is tilted and is fixed on the inwall of the gasification pot simultaneously
Twist rise.
In a preferred embodiment of the present invention, the helical structure in the Cyclonic gasifying road is no less than one layer, the whirlwind
The sectional area in gasification road is not less than 1.1 times of the air intake interface sectional area.
The beneficial effects of the invention are as follows：The present invention can make full use of the lighter by-products class light oil in PETROLEUM PROCESSING,
Combustion gas is become by gasification.It is most outstanding to have the beneficial effect that：
（1）Heated using hot blast to oil plant, the heating process of oil plant, gasification and mixed null process are merged and set same
Standby middle completion, therefore, in terms of device fabrication, technological process is simplified, province has subtracted water-cycle heating, reduced equipment body
Product, reduces equipment manufacturing cost；In terms of aerogenesis effect, gasification rate is fast, yield is high；One a diameter of 1000 millimeters of gasification
Cylinder, 24 hours 12000 cubic metres of aerogenesis can be achieved；In terms of production safety, the danger that heating element heater heats to oil plant is eliminated
Property, ensure production safety；
（2）It is fixed to operating temperature, pressure, oil-feed and air intake than quantitative automatic control using programmable controller, make aerogenesis
Process safety is reliable, produces combustion gas high-quality stable, energy-conserving and environment-protective；
（3）Gas raw material processed is not limited to C5, can be by C after adjusting the parameters such as temperature, pressure and gas oil ratio by technological requirement6、
C7It is changed into the mixed air gas of lighter hydrocarbons Deng light hydrocarbon light oil.
Brief description of the drawings
Fig. 1 is the structural representation of a preferred embodiment of the present invention；
Fig. 2 is the top view in the Cyclonic gasifying road and oil feeding tube device in preferred embodiment shown in Fig. 1；
Fig. 3 is Fig. 2 front view；
Fig. 4 is the structural representation of oil inlet pipe and oil plant mouth spray in preferred embodiment shown in Fig. 1.
The mark of each part is as follows in accompanying drawing：1st, gasification pot, 2, hot blast buffering pressure stabilizing chamber, 3, Cyclonic gasifying road, 4, oil plant
Variable pump, the 5, first check valve, 6, oil-feed interface tube, 7, oil inlet pipe, 8, oil plant mouth spray, 9, air inlet valve interface, 10, hot blast becomes
Measure pump, the 11, second check valve, 12, mixed empty room, 13, oily foam separator, 14, gas and oil separating plant, 15, anti-static mesh, 16,
Air storage chamber, 17, safety valve, 18, pressure sensor, 19, thermocouple, 20, gas outlet valve interface, 21, blowoff valve interface, 22,
Cylinder footing.
Embodiment
Presently preferred embodiments of the present invention is described in detail below in conjunction with the accompanying drawings, so that advantages and features of the invention energy
It is easier to be readily appreciated by one skilled in the art, apparent is clearly defined so as to be made to protection scope of the present invention.
A kind of liquid light hydrocarbon gasification installation, including gasification pot 1, oil plant variable pump 4, hot blast variable pump 10 and PLC technology
Device, the top of the outer barrel of gasification pot 1 are provided with gas outlet valve interface 20, safety valve 17, thermocouple 19 and pressure sensor 18, gas
The middle and lower part for changing the outer barrel of cylinder 1 is equipped with oil feeding device and air-intake device, and the bottom of gasification pot 1 is provided with blowoff valve interface 21, cylinder
Footing 22 and ground connection；The chamber of lower section buffers pressure stabilizing chamber 2 for hot blast in gasification pot 1, and the top of hot blast buffering pressure stabilizing chamber 2 is equipped with rotation
General mood road 3, the entrance in Cyclonic gasifying road 3 communicates with hot blast buffering pressure stabilizing chamber 2, and is provided with oil inlet pipe 7 and oil plant mouth spray
8, the outlet in Cyclonic gasifying road 3 communicates with mixed empty room 12；The mixed top of empty room 12 is oily foam separator 13 and gas and oil separating plant
14, the top that Oil-gas Separation fills 14 is air storage chamber 16, and anti-static mesh 15 is provided with air storage chamber 16.
Gasification pot 1 and internal structure, are the technological core parts of the present invention, and its effect is by light hydrocarbon liquid gasification, mixed
Space-variant is light-hydrocarbon gas.According to the gas fired-boiler tonnage and thermal hardware of different user, gas consumption, setting technology ginseng are calculated
Number, quantitatively input hot-air and C5Oil plant, air-fuel mixture proportioning automatically control hot blast variable pump 10 and oil plant variable using programming
Pump 4 realizes that the pressure in work system uses intelligent automatic control with temperature.
Oil feeding device includes the first check valve 5, oil-feed interface tube 6, oil inlet pipe 7 and oil plant mouth spray 8, the one end of oil inlet pipe 7
Stretched into by oil-feed interface tube 6 in the Cyclonic gasifying road 3 in gasification pot 1, stretching on the tube wall of oil inlet pipe 7 in Cyclonic gasifying road 3 has
Some oil plant mouth sprays 8 are evenly distributed with, the other end of oil inlet pipe 7 connects with the first check valve 5, the first check valve 5 and oil plant
Variable pump 4 is connected, and oil plant variable pump 4 is electrically connected with programmable controller.
Air-intake device includes the second check valve 11 and air inlet valve interface 9, and gasification is connected in one end of described air inlet valve interface 9
Hot blast buffering pressure stabilizing chamber 2 in cylinder 1, the other end connect with the second check valve 11, and the other end and the hot blast of the second check valve 11 become
Amount pump 10 is connected, and hot blast variable pump 10 is electrically connected with programmable controller.
Following is the specific structure of each device and parameter：
The gasification pot 1, is manufactured using model Q235B steel, and operating temperature is 40 DEG C ~ 45 DEG C, work pressure
Power is 0.035 ~ 0.045Mpa, belongs to normal temperature and pressure, but to ensure safety, according to the standard design of II type III pressure vessels, is manufactured,
And through pressure testing more than carrying out flaw detection and three times operating pressure, do not reveal within 24 hours.
The hot blast buffers pressure stabilizing chamber 2, and by programming setting air quantity, pressure, temperature parameter, heat is automatically controlled by controller
Wind variable pump 10, hot-air is quantified, level pressure, constant temperature are sent into.
The Cyclonic gasifying road 3, made using H62 brass, the design of Cyclonic gasifying road 3 uses apsacline, is fixed on gasification
On the inwall of cylinder 1 and spiral shape rises, and can have one or more layers, and it is to extend vaporization time, extension gasification space that it, which is acted on,
Make oil plant C5Fully gasification；The sectional area in Cyclonic gasifying road 3 is not less than 1.1 times of the sectional area of air intake interface 9.
The oil plant variable pump 4, the commercially available prod to match is chosen according to the design requirement of gas production.Oil plant variable pump 4
It is electrically connected with controller, its working condition cooperates with hot blast variable pump 10, by programming Control.
The check valve 11 of first check valve 5 and second, is respectively arranged in oil feeding device and air-intake device, will by technique
The technical parameter asked chooses the commercially available prod to match, and its effect is：Prevent mixed gas from flowing backwards during shutdown.
The oil-feed interface tube 6, is manufactured using model Q235B steel.
The oil inlet pipe 7, made using No. 20 seamless steel pipes, according to the air consumption of different user, calculated, setting oil inlet pipe
7 size, it is quantitative by oil plant C5Input, Cyclonic gasifying road 3 is entered by mouth spray 8.
The oil plant mouth spray 8, there is several, and all mouth sprays are uniformly distributed on the tube wall of oil inlet pipe 7.Each oil plant spray
A diameter of 1.2 ~ 1.3mm of mouth 8, quantity is then depending on the size of oil inlet pipe 7, and the area sum of all oil plant mouth sprays 8 is with entering
The area equation of oil pipe 7 is optimal.The diameter of oil plant mouth spray 8 is too small or quantity very little, oil plant can be sprayed, produce electrostatic, and
It is unfavorable for gasifying；Conversely, then can not fully dispersed oil plant, be also unfavorable for gasifying.
The air inlet valve interface 9, buffered after air is heated by the temperature, pressure, flow of setting through this mouth into hot blast
In pressure stabilizing chamber 2, size and the gas production of bore match.
The hot blast variable pump 10, the commercially available prod to match is chosen according to the design requirement of gas production.The pump and control
Device electrically connects, and its working condition cooperates with above-mentioned oil plant variable pump 4, by programming Control.The thermal source of required hot blast can utilize user
Waste heat, but still need to have electric heating wind apparatus, in just in the case where lacking waste heat（When being started such as gasification installation）Use.
The mixed empty room 12, made using H62 brass, oil plant is gasified and is mixed into mixed empty lighter hydrocarbons with air proportion and is fired
Gas.
The oily foam separator 13, gas and oil separating plant 14, using H62 brass make, in gasification by oil with
Qi leel from, and make mixed gas when by the device aggregation, be sufficiently mixed and accelerate flow velocity, into air storage chamber 16 after scatter,
Realize oil plant gasification, mix empty optimum state.
The anti-static mesh 15, made using H62 brass screens, can prevent that mixed airflow produces electrostatic during gasification, it is ensured that raw
Gas safety.
The air storage chamber 16, the light-hydrocarbon gas made by mixed empty room 12 is temporarily stored into this.
The safety valve 17, the commercially available prod to match is chosen by the technical parameter of technological requirement.
The pressure sensor 18 and thermocouple 19, choose commercially available prod.By electrically connecting gaseous mixture in air storage chamber 16
Temperature and wind of the pressure and temperature information transmission of body to programmable controller, the accordingly hot blast that control hot blast variable pump 10 is exported
Amount, and then control the temperature and pressure of light-hydrocarbon gas in air storage chamber 16.
The air outlet valve interface 20, manufactured light-hydrocarbon gas is supplied into gas-fired equipment through this interface, the size of bore is with entering
Air-valve interface 9 is equal.
The blowoff valve interface 21, in long-term gas-making process, there are a small amount of resin, accumulation of impurities, can be periodically from this
Mouth discharge.
The cylinder footing 22, including ground connection, the height of cylinder footing 22 are advisable in order to blowdown operation；Earthing material and
Installation meets specification.
The basic functional principle of the present invention：
When liquid light hydrocarbon reaches boiling temperature, constantly it will be changed into gaseous state from liquid., will be a small amount of according to this principle
Light hydrocarbon light oil is placed in substantial amounts of hot-air whirlwind field, when air themperature reaches oil plant boiling temperature, oil plant gasification, simultaneously
Mixed sky turns into light-hydrocarbon gas.Accordingly, the bottom of gasification pot 1 that the present invention designs is semiglobe, as shown in figure 1, composition hot blast delays
Pressure stabilizing chamber 2 is rushed, its top is hot blast Cyclonic gasifying road 3, and the air inlet in the gasification road communicates with hot blast buffering pressure stabilizing chamber 2, hot blast
Make circular flow distribution herein, enter Cyclonic gasifying road 3 from cylinder body bottom with tangential direction, form the rotary wind of higher wind
.The controlled quatity of oil plant by a certain percentage is gone out by mouth spray 8, enters mixed empty room 12 through Cyclonic gasifying road 3, in centrifugal force, shearing
Under the collective effect of power, impact force and heating power, oil plant fully contacts to form mixed air by micronized, gasification, and with rotation hot blast
State, through oily foam separator 13 and gas and oil separating plant 14, into air storage chamber 16.
Present invention is disclosed a kind of liquid light hydrocarbon gasification installation, is gasificated into light hydrocarbon light oil fast boiling using hot blast
Empty light-hydrocarbon gas is mixed, aerogenesis equipment volume is small, and yield is high, and input is small, and production cost is low.Temperature, pressure in gas-made technology flow
Power, flow, gas oil ratio etc. use programming Control, make production safer, quality is more stable.
Embodiments of the invention are the foregoing is only, are not intended to limit the scope of the invention, it is every to utilize this hair
The equivalent structure or equivalent flow conversion that bright specification and accompanying drawing content are made, or directly or indirectly it is used in other related skills
Art field, is included within the scope of the present invention.
Claims (7)
1. a kind of liquid light hydrocarbon gasification installation, including gasification pot（1）, oil plant variable pump（4）, hot blast variable pump（10）With it is programmable
Controller, it is characterised in that the gasification pot（1）The top of outer barrel is provided with gas outlet valve interface（20）, safety valve（17）、
Thermocouple（19）And pressure sensor（18）, the gasification pot（1）The middle and lower part of outer barrel is equipped with oil feeding device and air-intake device, institute
State gasification pot（1）Bottom blowoff valve interface is installed（21）, cylinder footing（22）And ground connection；The gasification pot（1）Interior lower section
Chamber for hot blast buffer pressure stabilizing chamber（2）, the hot blast buffering pressure stabilizing chamber（2）Top Cyclonic gasifying road is housed（3）, the rotation
General mood road（3）Entrance and hot blast buffering pressure stabilizing chamber（2）Communicate, and oil inlet pipe is installed（7）And oil plant mouth spray（8）, institute
State Cyclonic gasifying road（3）Outlet and mixed empty room（12）Communicate；The mixed empty room（12）Top is oily foam separator（13）With
Gas and oil separating plant（14）, the gas and oil separating plant（14）Top be air storage chamber（16）, the air storage chamber（16）Interior installation
There is anti-static mesh（15）；
The oil feeding device includes the first check valve（5）, oil-feed interface tube（6）, oil inlet pipe（7）With oil plant mouth spray（8）, it is described
Oil inlet pipe（7）One end passes through oil-feed interface tube（6）Stretch into the gasification pot（1）Interior Cyclonic gasifying road（3）In, stretch into the rotation
General mood road（3）The oil inlet pipe（7）Some oil plant mouth sprays are evenly distributed with tube wall（8）, the oil inlet pipe（7）It is another
One end and the first check valve（5）Connect, first check valve（5）With oil plant variable pump（4）Connection, the oil plant variable pump
（4）It is electrically connected with programmable controller；
The air-intake device includes the second check valve（11）With air inlet valve interface（9）, described air inlet valve interface（9）A termination
Hot blast buffering pressure stabilizing chamber in logical gasification pot（2）, the other end and the second check valve（11）Connect, second check valve（11）'s
The other end and hot blast variable pump（10）Connection, the hot blast variable pump（10）It is electrically connected with programmable controller.
2. liquid light hydrocarbon gasification installation according to claim 1, it is characterised in that the oil plant mouth spray（8）Diameter
No more than 1 .5mm, some oil plant mouth sprays（8）Sectional area sum be not more than the oil inlet pipe（7）Sectional area.
3. liquid light hydrocarbon gasification installation according to claim 1, it is characterised in that the air inlet valve interface（9）Bore
With gas outlet valve interface（20）Bore it is equal.
4. liquid light hydrocarbon gasification installation according to claim 1, it is characterised in that the pressure sensor（18）Probe
Stretch into the gasification pot（1）Interior air storage chamber（16）In, and by the air storage chamber（16）Interior pressure information passes through electric connection
It is transferred to the programmable controller.
5. liquid light hydrocarbon gasification installation according to claim 1, it is characterised in that the thermocouple（19）Probe stretch into
The gasification pot（1）Interior air storage chamber（16）In, and by the air storage chamber（16）Interior temperature information is transmitted by being electrically connected with
To the programmable controller.
6. liquid light hydrocarbon gasification installation according to claim 1, it is characterised in that the Cyclonic gasifying road（3）Tilt solid
Due to the gasification pot（1）Inwall on and twist rise.
7. liquid light hydrocarbon gasification installation according to claim 6, it is characterised in that the Cyclonic gasifying road（3）Spiral
Structure is no less than one layer, the Cyclonic gasifying road（3）Sectional area be not less than air inlet valve interface（9）1 .1 times of sectional area.
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| CN201610130778.3A CN105642195B (en) | 2016-03-09 | 2016-03-09 | A kind of liquid light hydrocarbon gasification installation |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN106244271A (en) * | 2016-08-19 | 2016-12-21 | 钱维洁 | The mixed empty control system of flash distillation |
| CN110242862B (en) * | 2019-06-26 | 2024-05-10 | 杨长喜 | Gas generating equipment |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN2314243Y (en) * | 1997-10-20 | 1999-04-14 | 齐斌 | Light oil combustor |
| DE19810536A1 (en) * | 1998-03-11 | 1999-09-16 | Linde Ag | Water bath evaporator for liquefied gases |
| CN2318536Y (en) * | 1998-04-09 | 1999-05-12 | 杨祥森 | 'Light hydrocarbon civil fuel' normal temp. high-efficient constant-ratio gasification device |
| CN201930557U (en) * | 2011-01-13 | 2011-08-17 | 王静 | Light hydrocarbon gasification and evaporation kettle and high-pressure bubbling gas production and transmission system |
| CN104456605B (en) * | 2014-12-08 | 2017-01-11 | 安徽启东热能科技有限公司 | Gasification device for ordinary-pressure liquid light hydrocarbons |
| CN205586958U (en) * | 2016-03-09 | 2016-09-21 | 常熟吉南贸易有限公司 | Liquid light hydrocarbon gasification equipment |
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