CN105642195A - Liquid-state light dydrocarbon gasifying device - Google Patents
Liquid-state light dydrocarbon gasifying device Download PDFInfo
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- CN105642195A CN105642195A CN201610130778.3A CN201610130778A CN105642195A CN 105642195 A CN105642195 A CN 105642195A CN 201610130778 A CN201610130778 A CN 201610130778A CN 105642195 A CN105642195 A CN 105642195A
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- oil
- gasifying
- variable pump
- air
- gasification
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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
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- 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
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- 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)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Feeding And Controlling Fuel (AREA)
Abstract
The invention discloses a liquid-state light dydrocarbon gasifying device which is capable of gasifying light dydrocarbon type light oil with C5-C6 and the like into combustible gas to provide novel clean energy for industrial and civil application. The liquid-state light dydrocarbon gasifying device mainly comprises a gasifying drum, an oil variable pump, a hot air variable pump and a programmable logic controller. An oil inlet device, an air inlet device, a safety valve, a pressure sensor, a thermocouple, a combustible gas outlet valve connector, a sewage valve connector, bottom studs of a drum body and a grounding connector are mounted on the gasifying drum. The gasifying drum is internally provided with a hot air buffering and pressure stabilizing chamber, a cyclone gasifying passage, an air mixing chamber, an oil foam separation device, a gas storage chamber and an anti-static net. Quantitative constant-temperature constant-proportion supply of oil and hot air is realized by the oil variable pump and the hot air variable pump, the oil variable pump and the hot air variable pump are automatically controlled by the controller, and the oil and the hot air are gasified through the gasifying drum to obtain air mixed combustible gas. The liquid-state light dydrocarbon gasifying device enables stable quality, yield increase, manufacturing cost reduction and size reduction of gas generation equipment, and energy saving and environment friendliness are realized.
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, mixes with air by a certain percentage simultaneously, forms the device of mixing gas. For the light hydrocarbon light oil of gas processed, mainly C5(carbon five), C6(carbon six) and C7(carbon seven) etc. At present, it is possible to by C5(carbon five) is gaseous state from liquid state, and is mixed to form fuel gas with air, for people to use. But the drawbacks such as existing gasification installation exists poor stability, the efficiency of heating surface is low, equipment volume is big, gas production is little and produced combustion gas quality is unstable.
Existing one " liquid C 5 vaporisation apparatus " (patent No.: ZL200720037587.9), uses " still the heating element heater of daily seen immersion heater, insulating pot ", is inserted into by this heating element heater and heats to oil plant equipped with after energising in the tank chamber of oil plant. So heating, is absolutely unsafe, it may occur that major accident. In routine use, even if heating element heater is placed in jacket pipe, it is also difficult to stop potential safety hazard, and substantially reduce the efficiency of heating surface.
Now separately there is one " liquid C 5 vaporisation apparatus " (patent of invention number: ZL200910182911.X; Utility model patent Authorization Notice No.: CN201502867U), adopt one group of heating element heater to adding thermal medium (water) heating, and by medium (water) oil plant heat transfer in tank skin is to tank. Heating energy consumption is high, efficiency is low for it, and device structure is complicated, volume is big, gas production is little.
Now also have a kind of " the mixed empty light hydrogen cracking still of high energy " (number of patent application: 201510538133.9), using PLC Based Intelligent Control, light hydrocarbon light oil is heated Bubbler vaporizer, is mixed to form fuel gas with air simultaneously. But also fail to solve the problems such as the efficiency of heating surface is low, equipment volume is big, gas production is little and combustion gas quality is unstable. Its control system does not include the mixing match of oil plant and air in span of control, fails the control best, effectively, at any time realized oil plant and air stoichiometry.
Three of the above prior art, is all utilize C5(carbon five) low-boiling characteristic is heated Bubbler vaporizer, is mixed to form the mixed air-fuel gas of lighter hydrocarbons with air.But in the mixed air-fuel gas of lighter hydrocarbons, light hydrocarbon light oil proportion deficiency one thousandth, other are all air, therefore, only to oil plant heating it is difficult to ensure that normal gas producing, especially in the winter time, being mixed into of a large amount of cold airs, reducing the gasification of heats, suppression oil plant, the quality of its produced combustion gas is difficult to stable. Further, owing to heats is poor, gas raw material processed is confined to the C that boiling point is relatively low5, it is impossible to by C6��C7Combustion gas is turned to Deng light petroleum gas. Additionally, the technology of the mixed air-fuel gas of existing production lighter hydrocarbons, all failing effectively to control the mixing match of oil plant and air, fail to realize the weight feed of oil plant, energy-saving effect is not good enough.
Summary of the invention
The technical problem that present invention mainly solves is to provide a kind of liquid light hydrocarbon gasification installation, cost and aerogenesis cost can be reduced, save energy consumption, ensure production safety, stablize aerogenesis quality, improve gas production, produced combustion gas can substitute natural gas, liquefied gas and coal, for industrial and civilian offer heat energy, energy-saving and environment-friendly.
For solving above-mentioned technical problem, the technical scheme that the present invention adopts is:
A kind of liquid light hydrocarbon gasification installation is provided, including gasification pot, oil plant variable pump, hot blast variable pump and Programmable Logic Controller, the top of described gasification pot urceolus is provided with gas outlet valve interface, relief valve, thermocouple and pressure transducer, the middle and lower part of described gasification pot urceolus is equipped with oil feeding device and air-intake device, and the bottom of described gasification pot is provided with blowoff valve interface, cylinder footing and ground connection; In described gasification pot, the chamber of lower section is hot blast buffering pressure stabilizing chamber, the top of described hot blast buffering pressure stabilizing chamber is equipped with Cyclonic gasifying road, the entrance in described Cyclonic gasifying road cushions pressure stabilizing chamber with hot blast and communicates, and oil inlet pipe and oil plant mouth spray are installed, the outlet in described Cyclonic gasifying road communicates with mixed empty room; Described mixed empty top, room is that described in oil foam segregation apparatus and gas and oil separating plant, the top of gas and oil separating plant is air storage chamber, is provided with anti-static mesh in described air storage chamber.
In a preferred embodiment of the present invention, described oil feeding device includes the first check valve, oil inlet pipe interface, oil inlet pipe and oil plant mouth spray, described oil inlet pipe one end is stretched in the Cyclonic gasifying road in described gasification pot by oil inlet pipe interface, stretch into and the described oil inlet pipe tube wall in described Cyclonic gasifying road is evenly distributed with some oil plant mouth sprays, the other end and first check valve of described oil inlet pipe connect, described first check valve is connected with oil plant variable pump, and described oil plant variable pump is electrically connected with Programmable Logic Controller.
In a preferred embodiment of the present invention, the diameter of described oil plant mouth spray is not more than 1.5mm, and described some mouth spray sectional area sums are not more than the sectional area of described oil inlet pipe.
In a preferred embodiment of the present invention, described air-intake device includes the second check valve and air inlet valve interface, the hot blast buffering pressure stabilizing chamber in gasification pot is connected in one end of described air inlet valve interface, the other end and the second check valve connect, the other end of described second check valve is connected with hot blast variable pump, and described hot blast variable pump is electrically connected with Programmable Logic Controller.
In a preferred embodiment of the present invention, the bore of described air inlet valve interface is equal with the bore of gas outlet valve interface.
In a preferred embodiment of the present invention, the probe of described pressure transducer stretches in the air storage chamber in described gasification pot, and by electric connection, the pressure information in described air storage chamber is transferred to described Programmable Logic Controller.
In a preferred embodiment of the present invention, the probe of described thermocouple stretches in the air storage chamber in described gasification pot, and by electric connection, the temperature information in described air storage chamber is transferred to described Programmable Logic Controller.
In a preferred embodiment of the present invention, described Cyclonic gasifying road tilts be fixed on the inwall of described gasification pot and rise twist.
In a preferred embodiment of the present invention, the helical structure in described Cyclonic gasifying road is no less than one layer, and the sectional area in described Cyclonic gasifying road is not less than 1.1 times of described air intake interface sectional area.
The invention has the beneficial effects as follows: the present invention can make full use of the lighter by-products class light oil in PETROLEUM PROCESSING, become combustion gas by gasifying. Its most outstanding having the beneficial effect that
(1) adopt hot blast to heat to oil plant, the heating process of oil plant, gasification and mixed null process are merged and completes in same equipment, therefore, in device fabrication, simplify technological process, economized and subtracted water-cycle heating, reduce equipment volume, reduce equipment manufacturing cost; In aerogenesis effect, gasification rate is fast, yield is high; One diameter is the gasification pot of 1000 millimeters, it may be achieved 24 hours aerogenesis 12000 cubic metres; In production safety, eliminate the danger that oil plant is heated by heating element heater, ensured production safety;
(2) adopt Programmable Logic Controller to operating temperature, pressure, oil-feed and the quantitative automatic control of air intake definite proportion, make gas generation process safe and reliable, produced combustion gas high-quality stable, energy-conserving and environment-protective;
(3) gas raw material processed is not limited to C5, adjust the parameters such as temperature, pressure and gas oil ratio by technological requirement after, can by C6��C7It is changed into the mixed air-fuel gas of lighter hydrocarbons Deng light hydrocarbon light oil.
Accompanying drawing explanation
Fig. 1 is the structural representation of a preferred embodiment of the present invention;
Fig. 2 is the top view of the Cyclonic gasifying road in preferred embodiment shown in Fig. 1 and oil feeding tube device;
Fig. 3 is the front view of Fig. 2;
Fig. 4 is the structural representation of oil inlet pipe and oil plant mouth spray in preferred embodiment shown in Fig. 1.
In accompanying drawing, the labelling of each parts is as follows: 1, gasification pot, 2, hot blast buffering pressure stabilizing chamber, 3, Cyclonic gasifying road, 4, oil plant variable pump, 5, first check valve, 6, oil inlet pipe interface, 7, oil inlet pipe, 8, oil plant mouth spray, 9, air inlet valve interface, 10, hot blast variable pump, 11, second check valve, 12, mixed empty room, 13, oil foam segregation apparatus, 14, gas and oil separating plant, 15, anti-static mesh, 16, air storage chamber, 17, relief valve, 18, pressure transducer, 19, thermocouple, 20, gas outlet valve interface, 21, blowoff valve interface, 22, cylinder footing.
Detailed description of the invention
Below in conjunction with accompanying drawing, presently preferred embodiments of the present invention is described in detail, so that advantages and features of the invention can be easier to be readily appreciated by one skilled in the art, thus protection scope of the present invention being made apparent clear and definite defining.
A kind of liquid light hydrocarbon gasification installation, including gasification pot 1, oil plant variable pump 4, hot blast variable pump 10 and Programmable Logic Controller, the top of gasification pot 1 urceolus is provided with gas outlet valve interface 20, relief valve 17, thermocouple 19 and pressure transducer 18, the middle and lower part of gasification pot 1 urceolus 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; In gasification pot 1, the chamber of lower section is hot blast buffering pressure stabilizing chamber 2, the top of hot blast buffering pressure stabilizing chamber 2 is equipped with Cyclonic gasifying road 3, the entrance in Cyclonic gasifying road 3 cushions pressure stabilizing chamber 2 with hot blast and communicates, and is provided with oil inlet pipe 7 and oil plant mouth spray 8, and the outlet in Cyclonic gasifying road 3 communicates with mixed empty room 12;Mixed empty top, room 12 is oil foam segregation apparatus 13 and gas and oil separating plant 14, and it is air storage chamber 16 that Oil-gas Separation fills the top of 14, is provided with anti-static mesh 15 in air storage chamber 16.
Gasification pot 1 and internal structure, be the technological core part of the present invention, and its effect is to be light-hydrocarbon gas by light hydrocarbon liquid gasification, mixed space-variant. Gas fired-boiler tonnage according to different user and thermal hardware, calculate gas consumption, sets technical data, quantitatively input hot-air and C5Oil plant, air-fuel mixture proportioning adopts programming to automatically control hot blast variable pump 10 and oil plant variable pump 4 realizes, and the pressure in work system adopts intelligent automatic control with temperature.
Oil feeding device includes the first check valve 5, oil inlet pipe interface 6, oil inlet pipe 7 and oil plant mouth spray 8, oil inlet pipe 7 one end is stretched in the Cyclonic gasifying road 3 in gasification pot 1 by oil inlet pipe interface 6, stretch into and oil inlet pipe 7 tube wall in Cyclonic gasifying road 3 is evenly distributed with some oil plant mouth sprays 8, the other end and first check valve 5 of oil inlet pipe 7 connect, first check valve 5 is connected with oil plant variable pump 4, and oil plant variable pump 4 is electrically connected with Programmable Logic Controller.
Air-intake device includes the second check valve 11 and air inlet valve interface 9, the hot blast buffering pressure stabilizing chamber 2 in gasification pot 1 is connected in one end of described air inlet valve interface 9, the other end and the second check valve 11 connect, the other end of the second check valve 11 is connected with hot blast variable pump 10, and hot blast variable pump 10 is electrically connected with Programmable Logic Controller.
The following structure concrete for each device and parameter:
Described gasification pot 1, the steel adopting model to be Q235B manufacture, operating temperature is 40 DEG C ~ 45 DEG C, operating pressure is 0.035 ~ 0.045Mpa, belong to normal temperature and pressure, but for guaranteeing safety, design according to the standard of II type III pressure vessel, manufacture, and the pressure testing more than carrying out flaw detection and three times of operating pressures, within 24 hours, do not reveal.
Described hot blast buffering pressure stabilizing chamber 2, sets air quantity, pressure, temperature parameter by programming, controller automatically controls hot blast variable pump 10, and hot-air is quantitative, level pressure, constant temperature are sent into.
Described Cyclonic gasifying road 3, adopts H62 pyrite to make, and Cyclonic gasifying road 3 is designed with apsacline, is fixed on the inwall of gasification pot 1 and spiral type rises, it is possible to have one or more layers, and its effect is prolongation vaporization time, extends gasification space, makes oil plant C5Fully gasification; The sectional area in Cyclonic gasifying road 3 is not less than 1.1 times of air intake interface 9 sectional area.
Described oil plant variable pump 4, chooses the commercially available prod matched according to the designing requirement of gas production. Oil plant variable pump 4 is electrically connected with controller, and its duty is worked in coordination with hot blast variable pump 10, by programming Control.
Described first check valve 5 and the second check valve 11, is respectively arranged in oil feeding device and air-intake device, chooses the commercially available prod matched by the technical parameter of technological requirement, and its effect is: prevent mixing gas backflow during shutdown.
Described oil inlet pipe interface 6, the steel adopting model to be Q235B manufacture.
Described oil inlet pipe 7, adopts No. 20 seamless steel pipes to make, and the air consumption according to different user calculates, sets the size of oil inlet pipe 7, quantitatively by oil plant C5Input, enters Cyclonic gasifying road 3 by mouth spray 8.
Described oil plant mouth spray 8, has several, and all mouth sprays are uniformly distributed on oil inlet pipe 7 tube wall. The diameter of each oil plant mouth spray 8 is 1.2 ~ 1.3mm, and quantity is then determined according to the size of oil inlet pipe 7, and the area sum of all oil plant mouth sprays 8 and oil inlet pipe 7 area equation are best.The diameter of oil plant mouth spray 8 is too little or quantity very little, oil plant can be made to spray, produce electrostatic, and be unfavorable for gasification; Otherwise, then can not fully dispersed oil plant, also be unfavorable for gasification.
Described air inlet valve interface 9, enters in hot blast buffering pressure stabilizing chamber 2 through this mouth by the temperature set, pressure, flow after air is heated, and the size of bore and gas production match.
Described hot blast variable pump 10, chooses the commercially available prod matched according to the designing requirement of gas production. This pump is electrically connected with the controller, and its duty is worked in coordination with above-mentioned oil plant variable pump 4, by programming Control. The waste heat of the available user of thermal source of required hot blast, but still need to have electric hot-air device, in just (when starting such as the gasification installation) use when lacking waste heat.
Described mixed empty room 12, adopts H62 pyrite to make, and is mixed into empty light-hydrocarbon gas by oil plant gasification and with air proportion.
Described oil foam segregation apparatus 13, gas and oil separating plant 14, adopt H62 pyrite to make, in gasification by oil and edema caused by disorder of QI from, and make mixing gas through the gathering of this device, be sufficiently mixed and accelerate flow velocity, scatter after entering air storage chamber 16, it is achieved oil plant gasification, mixed empty optimum state.
Described anti-static mesh 15, adopts H62 brass screen to make, and when can prevent from gasifying, mixed airflow produces electrostatic, it is ensured that angry safety.
Described air storage chamber 16, is temporarily stored into this by the light-hydrocarbon gas made by mixed empty room 12.
Described relief valve 17, chooses the commercially available prod matched by the technical parameter of technological requirement.
Described pressure transducer 18 and thermocouple 19, choose commercially available prod. By electrically connecting, the pressure and temperature information of mixing gas in air storage chamber 16 is sent to programmable controller, controls temperature and the air quantity of the hot blast that hot blast variable pump 10 exports accordingly, and then control the temperature and pressure of light-hydrocarbon gas in air storage chamber 16.
Described air outlet valve interface 20, supplies gas-fired equipment by the light-hydrocarbon gas made through this interface, and the size of bore is equal with air inlet valve interface 9.
Described blowoff valve interface 21, in long-term gas-making process, has a small amount of resin, accumulation of impurities, can regularly from then on mouth discharge.
Described cylinder footing 22, including ground connection, the height of cylinder footing 22 is so that blowdown operation is advisable; Earthing material and installation compliant.
The basic functional principle of the present invention:
When liquid light hydrocarbon reaches boiling temperature, will constantly from liquid state be gaseous state. According to this principle, being placed in by a small amount of light hydrocarbon light oil in substantial amounts of hot-air whirlwind field, when air themperature reaches oil plant boiling temperature, oil plant gasifies, and mixed sky becomes light-hydrocarbon gas simultaneously. Accordingly, it is semiglobe bottom the gasification pot 1 of present invention design, as shown in Figure 1, composition hot blast buffering pressure stabilizing chamber 2, its top is hot blast Cyclonic gasifying road 3, and the air inlet in this gasification road cushions pressure stabilizing chamber 2 with hot blast and communicates, and hot blast makes circular flow distribution at this, enter Cyclonic gasifying road 3 from cylinder body bottom with tangential direction, form the rotation wind field of higher wind. Oil plant controlled quatity by a certain percentage is gone out by mouth spray 8; mixed empty room 12 is entered through Cyclonic gasifying road 3; under the combined effect of centrifugal force, shearing force, impact force and heating power; oil plant is by micronized, gasification; and it is fully contacted the mixed air state of formation with rotating hot blast; through oil foam segregation apparatus 13 and gas and oil separating plant 14, enter air storage chamber 16.
Present invention is disclosed a kind of liquid light hydrocarbon gasification installation, adopt hot blast that light hydrocarbon light oil fast boiling is gasificated into mixed empty light-hydrocarbon gas, aerogenesis equipment volume is little, and yield is high, puts into little, and production cost is low.Temperature in gas-made technology flow process, pressure, flow, gas oil ratio etc. adopt programming Control, make production safer, and quality is more stable.
The foregoing is only embodiments of the invention; not thereby the scope of the claims of the present invention is limited; every equivalent structure utilizing description of the present invention and accompanying drawing content to make or equivalence flow process conversion; or directly or indirectly it is used in other relevant technical fields, all in like manner include in the scope of patent protection of the present invention.
Claims (9)
1. a liquid light hydrocarbon gasification installation, including gasification pot (1), oil plant variable pump (4), hot blast variable pump (10) and Programmable Logic Controller, it is characterized in that, the top of described gasification pot (1) urceolus is provided with gas outlet valve interface (20), relief valve (17), thermocouple (19) and pressure transducer (18), the middle and lower part of described gasification pot (1) urceolus is equipped with oil feeding device and air-intake device, and the bottom of described gasification pot (1) is provided with blowoff valve interface (21), cylinder footing (22) and ground connection; In described gasification pot (1), the chamber of lower section is hot blast buffering pressure stabilizing chamber (2), the top of described hot blast buffering pressure stabilizing chamber (2) is equipped with Cyclonic gasifying road (3), the entrance of described Cyclonic gasifying road (3) cushions pressure stabilizing chamber (2) with hot blast and communicates, and oil inlet pipe (7) and oil plant mouth spray (8) are installed, the outlet of described Cyclonic gasifying road (3) communicates with mixed empty room (12); Described mixed empty room (12) top is oil foam segregation apparatus (13) and gas and oil separating plant (14), and the top of described gas and oil separating plant (14) is air storage chamber (16), is provided with anti-static mesh (15) in described air storage chamber (16).
2. liquid light hydrocarbon gasification installation according to claim 1, it is characterized in that, described oil feeding device includes the first check valve (5), oil inlet pipe interface (6), oil inlet pipe (7) and oil plant mouth spray (8), described oil inlet pipe (7) one end is stretched in the Cyclonic gasifying road (3) in described gasification pot (1) by oil inlet pipe interface (6), stretch into and described oil inlet pipe (7) tube wall of described Cyclonic gasifying road (3) is evenly distributed with some oil plant mouth sprays (8), the other end and first check valve (5) of described oil inlet pipe (7) connect, described first check valve (5) is connected with oil plant variable pump (4), described oil plant variable pump (4) is electrically connected with Programmable Logic Controller.
3. liquid light hydrocarbon gasification installation according to claim 2, it is characterised in that the diameter of described oil plant mouth spray (8) is not more than 1.5mm, the sectional area sum of described some oil plant mouth sprays (8) is not more than the sectional area of described oil inlet pipe (7).
4. liquid light hydrocarbon gasification installation according to claim 1, it is characterized in that, described air-intake device includes the second check valve (11) and air inlet valve interface (9), hot blast buffering pressure stabilizing chamber (2) in gasification pot is connected in one end of described air inlet valve interface (9), the other end and the second check valve (11) connect, the other end of described second check valve (11) is connected with hot blast variable pump (10), and described hot blast variable pump (10) is electrically connected with Programmable Logic Controller.
5. liquid light hydrocarbon gasification installation according to claim 4, it is characterised in that the bore of described air inlet valve interface (9) is equal with the bore of gas outlet valve interface (20).
6. liquid light hydrocarbon gasification installation according to claim 1, it is characterized in that, the probe of described pressure transducer (18) stretches in the air storage chamber (16) in described gasification pot (1), and by electric connection, the pressure information in described air storage chamber (16) is transferred to described Programmable Logic Controller.
7. liquid light hydrocarbon gasification installation according to claim 1, it is characterized in that, the probe of described thermocouple (19) stretches in the air storage chamber (16) in described gasification pot (1), and by electric connection, the temperature information in described air storage chamber (16) is transferred to described Programmable Logic Controller.
8. liquid light hydrocarbon gasification installation according to claim 1, it is characterised in that described Cyclonic gasifying road (3) tilts be fixed on the inwall of described gasification pot (1) and rise twist.
9. liquid light hydrocarbon gasification installation according to claim 8, it is characterised in that the helical structure of described Cyclonic gasifying road (3) is no less than a layer, and the sectional area of described Cyclonic gasifying road (3) is not less than 1.1 times of described air intake interface (9) sectional area.
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106244271A (en) * | 2016-08-19 | 2016-12-21 | 钱维洁 | The mixed empty control system of flash distillation |
| CN110242862A (en) * | 2019-06-26 | 2019-09-17 | 杨长喜 | A kind of combustion gas generation equipment |
| CN114082314A (en) * | 2021-09-28 | 2022-02-25 | 中国大唐集团科学技术研究总院有限公司华东电力试验研究院 | Preparation system and method of oil-containing standard gas |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2314243Y (en) * | 1997-10-20 | 1999-04-14 | 齐斌 | Light oil combustor |
| CN2318536Y (en) * | 1998-04-09 | 1999-05-12 | 杨祥森 | 'Light hydrocarbon civil fuel' normal temp. high-efficient constant-ratio gasification device |
| DE19810536A1 (en) * | 1998-03-11 | 1999-09-16 | Linde Ag | Water bath evaporator for liquefied gases |
| 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 |
| CN104456605A (en) * | 2014-12-08 | 2015-03-25 | 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 |
-
2016
- 2016-03-09 CN CN201610130778.3A patent/CN105642195B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN104456605A (en) * | 2014-12-08 | 2015-03-25 | 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 |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106244271A (en) * | 2016-08-19 | 2016-12-21 | 钱维洁 | The mixed empty control system of flash distillation |
| CN110242862A (en) * | 2019-06-26 | 2019-09-17 | 杨长喜 | A kind of combustion gas generation equipment |
| CN110242862B (en) * | 2019-06-26 | 2024-05-10 | 杨长喜 | Gas generating equipment |
| CN114082314A (en) * | 2021-09-28 | 2022-02-25 | 中国大唐集团科学技术研究总院有限公司华东电力试验研究院 | Preparation system and method of oil-containing standard gas |
| CN114082314B (en) * | 2021-09-28 | 2024-06-11 | 中国大唐集团科学技术研究总院有限公司华东电力试验研究院 | Preparation system and method for oil-containing standard gas |
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| CN105642195B (en) | 2018-03-30 |
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Effective date of registration: 20201123 Address after: Block b-4-5-5, Tangji area, Jiangping Industrial Park, Dongxing City, Fangchenggang City, Guangxi Zhuang Autonomous Region Patentee after: Guangxi Dongxing Fujia hardware and leather goods Co., Ltd Address before: 1, 705, HSBC Times Plaza, 22 the Yellow River Road, Suzhou, Jiangsu, Changshou City 215500 Patentee before: CHANGSHU JINAN TRADING Co.,Ltd. |
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