CN208124347U - A kind of preparation facilities of mixed empty light-hydrocarbon gas - Google Patents
A kind of preparation facilities of mixed empty light-hydrocarbon gas Download PDFInfo
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- CN208124347U CN208124347U CN201820314994.8U CN201820314994U CN208124347U CN 208124347 U CN208124347 U CN 208124347U CN 201820314994 U CN201820314994 U CN 201820314994U CN 208124347 U CN208124347 U CN 208124347U
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- hydrogen cracking
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- light hydrogen
- cracking tank
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Abstract
The utility model discloses a kind of preparation facilities of mixed empty light-hydrocarbon gas, including light hydrogen cracking tank, lighter hydrocarbons storage tank, air blower, heating tube is equipped in light hydrogen cracking tank, air blower is equipped with the air inlet pipe for being connected to light hydrogen cracking tank, the end of air inlet pipe is close to light hydrogen cracking tank bottom wall, air inlet pipe runs through close to the position of light hydrogen cracking tank deck wall mounting hole, shaft is rotatably connected in mounting hole, the side wall that shaft is located inside air inlet pipe is provided with blade, one end outside air inlet pipe is provided with fan.The utility model has the following advantages that and effect：When system mixes empty lighter hydrocarbons, liquid light hydrocarbon in lighter hydrocarbons storage tank is pumped in light hydrogen cracking tank, liquid light hydrocarbon vaporizes after heating tube and forms steam state lighter hydrocarbons, air is blown into light hydrogen cracking tank by starting air blower along air inlet pipe, air blows blade and drives shaft and fan rotation, and then uniformly mixed mixed empty lighter hydrocarbons are made.Achieve the effect that the preparation process of mixed empty lighter hydrocarbons is convenient and efficient, be uniformly mixed.
Description
Technical field
The utility model relates to new energy to supply field, in particular to a kind of preparation facilities of mixed empty light-hydrocarbon gas.
Background technique
Light-hydrocarbon gas is novel environment friendly liquid fuel, be in petroleum, natural gas extraction and process byproduct C5,
C6 is gas raw material processed.Light-hydrocarbon gas is all clean fuel as natural gas, other than calorific value is high, burning and exhausting cleans, with day
Right gas is compared with liquefied petroleum gas, is transported, is stored, distributing more convenient safety, can be used as resident's diet, bathing, adopt
The public utilities such as the gas source of the various life gas facilities such as warm and organ, school, restaurant and the ideal for producing heating facility
Gas source.
The Chinese patent of authorization Publication No. CN201892224U discloses a kind of mixed empty light-hydrocarbon gas preparation of atomization and vaporization
Device, the device is by air compressor, liquid light hydrocarbon tank, automatically controlled liquid pressure regulator valve or liquid flow controller, atomizer
Fluidic interface, heat exchange atomization, gasifying pot and air accumulator are sequentially connected, another outlet of air compressor and automatically controlled gas pressure regulating valve
Or the input port connection of gas flow controller, the output port connection mist of automatically controlled gas pressure regulating valve or gas flow controller
Change the air interface of spray head；Using the method gasifying liquid lighter hydrocarbons of atomized liquid lighter hydrocarbons, and a certain proportion of air is mixed to make
Standby mixed empty light-hydrocarbon gas.
Above-mentioned mixed empty light hydrocarbon gas preparing device in the mixed empty lighter hydrocarbons of preparation needs that liquid light hydrocarbon is first pressed into atomizer
Fluidic interface, then compressed air is pressed into the fluidic interface of atomizer together, the lighter hydrocarbons being atomized at this time heat exchange atomization,
It vaporizes and is mixed with air in mixed empty lighter hydrocarbons in gasifying pot.The mixed empty lighter hydrocarbons process very complicated of preparation, and lighter hydrocarbons and air are mixed
Unevenness is closed, is had much room for improvement.
Utility model content
The purpose of the utility model is to provide a kind of preparation facilities of mixed empty light-hydrocarbon gas, have the preparation of mixed empty lighter hydrocarbons
Convenient and efficient, the uniformly mixed effect of journey.
The above-mentioned technical purpose of the utility model technical scheme is that：The mixed empty light-hydrocarbon gas of one kind
Preparation facilities, including light hydrogen cracking tank, lighter hydrocarbons storage tank, air blower, the lighter hydrocarbons storage tank be equipped be connected to it is described light
The connecting tube of hydrocarbon reaction tank lower end, light hydrogen cracking tank upper end are equipped with exhaust pipe, are equipped with middle position in the light hydrogen cracking tank
Inside the light hydrogen cracking tank and both ends are fed through after the light hydrogen cracking pot sidewall outside the light hydrogen cracking tank
Heating tube, the air blower are equipped with the air inlet pipe for being connected to the light hydrogen cracking tank, and the end of the air inlet pipe is close to described
Light hydrogen cracking tank bottom wall.
By using above-mentioned technical proposal, when needing to prepare mixed empty lighter hydrocarbons, by the liquid light hydrocarbon edge in lighter hydrocarbons storage tank
Connecting tube be pumped in light hydrogen cracking tank, then hot water is passed through in heating tube, by heat exchange principle to heating tube carry out
Heating, the liquid light hydrocarbon heat in light hydrogen cracking tank vaporizes to form steam state lighter hydrocarbons at this time.Then start air blower, air blower will be outer
The air on boundary is pumped into blast pipe, and after the filtering using air filtration core, air is blown into light hydrogen cracking tank along air inlet pipe
Interior, air and steam state lighter hydrocarbons are mixed into empty lighter hydrocarbons at this time, then mix empty lighter hydrocarbons and are discharged along exhaust pipe, user or burning at this time
Equipment is i.e. using mixed empty lighter hydrocarbons.Achieve the effect that the preparation process of mixed empty lighter hydrocarbons is convenient and efficient, be uniformly mixed.
The utility model is further arranged to：The air inlet pipe runs through close to the position of the light hydrogen cracking tank deck wall to be had
Mounting hole, is rotatably connected to shaft in the mounting hole, the side wall that the shaft is located inside the air inlet pipe be provided with blade,
One end outside the air inlet pipe is provided with fan.
By using above-mentioned technical proposal, when air blower blows air into air inlet pipe, the impact force of air impacts blade
Movement, blade drives shaft rotation at this time, and shaft drives fan rotation, the active force generated using fan rotation by air and
Steam state lighter hydrocarbons are uniformly mixed, and then form more uniform mixed empty lighter hydrocarbons.
The utility model is further arranged to：Sealing axis is provided between the shaft outer wall and the inner wall of the hole installing
It holds, the sealing bearing includes outer ring, inner ring, ball, and the inner ring is fixed on the shaft outer wall, the outer ring interference fit
With the inner wall of the hole installing.
By using above-mentioned technical proposal, the frictional force between shaft and mounting hole is reduced by setting bearing, is also reduced
The abrasion of shaft outer wall and inner wall of the hole installing.
The utility model is further arranged to：The outer ring, the inner ring have been coated with insulated paint on the ball.
By using above-mentioned technical proposal, insulation effect is played by the way that insulated paint is arranged, avoids outer ring, inner ring, ball phase
When to rotation, friction generates the initiation explosion of spark initiation lighter hydrocarbons between outer ring and ball, inner ring and ball.
The utility model is further arranged to：Barometric pipe, the air pressure are provided with outside the light hydrogen cracking tank
Balance pipe one end is connected to the light hydrogen cracking tank and the other end is connected to the air inlet pipe, is provided on the barometric pipe
The check valve flowed into the air inlet pipe for controlling the gas in the light hydrogen cracking tank.
By using above-mentioned technical proposal, when blowing air into air inlet pipe, the air in light hydrogen cracking tank is along air pressure
Balance pipe and check valve flow into air inlet pipe, keep light hydrogen cracking tank and the air pressure in the external world to locate always using barometric pipe
In equilibrium state, when avoiding that pressure is excessive in light hydrogen cracking tank, the liquid light hydrocarbon of light hydrogen cracking pot bottom is forced out.
The utility model is further arranged to：It is provided with blast pipe on the air blower, is provided in the blast pipe
Air filtration core.
It is avoided by using above-mentioned technical proposal by setting air filtration core by dust or contaminant filter in air
Dust or impurity pollute light hydrogen cracking tank.
The utility model is further arranged to：The lower end of the light hydrogen cracking tank is provided with sewage pipe, the sewage pipe
On be provided with valve.
By using above-mentioned technical proposal, a little impurity can be generated after the lighter hydrocarbons vaporization in light hydrogen cracking tank, when excessive miscellaneous
After matter accumulation, valve is opened, impurity can be discharged by the sewage pipe of light hydrogen cracking tank lower end, after impurity is removed,
Turn off valve.
The utility model is further arranged to：Light hydrogen cracking tank lower end surface is provided with stabilizer blade, sets on the stabilizer blade
It is equipped with the detector for detecting the flammable Gas content in air.
By using above-mentioned technical proposal, by the flammable Gas content in setting detector test air, when content is exceeded
When, alarm warning worker can occur for detector, avoid flammable Gas content is exceeded from exploding.
In conclusion the utility model has the advantages that：It, will be in lighter hydrocarbons storage tank when the mixed empty lighter hydrocarbons of preparation
Liquid light hydrocarbon is pumped in light hydrogen cracking tank, and liquid light hydrocarbon vaporizes after heating tube forms steam state lighter hydrocarbons, and starting air blower will
Air is blown into light hydrogen cracking tank along air inlet pipe, and air blows blade and drives shaft and fan rotation, and then mixing is made
Uniform mixed empty lighter hydrocarbons.Achieve the effect that the preparation process of mixed empty lighter hydrocarbons is convenient and efficient, be uniformly mixed.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of embodiment；
Fig. 2 is the positional diagram of embodiment；
Fig. 3 is the sealing bearing of embodiment, blade construction schematic diagram.
In figure：1, light hydrogen cracking tank；11, exhaust pipe；12, heating tube；13, sewage pipe；14, valve；15, stabilizer blade；16, it examines
Survey instrument；2, lighter hydrocarbons storage tank；21, connecting tube；3, air blower；31, air inlet pipe；311, mounting hole；312, shaft；313, blade；
314, fan；32, blast pipe；321, air filtration core；4, barometric pipe；41, check valve；5, bearing is sealed；51, outer ring；
52, inner ring；53, ball.
Specific embodiment
The utility model is described in further detail below in conjunction with attached drawing.
A kind of preparation facilities of mixed empty light-hydrocarbon gas, as shown in Figure 1 and Figure 2, including light hydrogen cracking tank 1, lighter hydrocarbons storage tank 2,
Air blower 3.Lighter hydrocarbons storage tank 2 is equipped with the connecting tube 21 for being connected to 1 lower end of light hydrogen cracking tank, and 1 upper end of light hydrogen cracking tank is equipped with
Exhaust pipe 11, is equipped with that middle part is located inside light hydrogen cracking tank 1 and both ends are fed through 1 side wall of light hydrogen cracking tank in light hydrogen cracking tank 1
The heating tube 12 being located at outside light hydrogen cracking tank 1 afterwards.Air blower 3 is equipped with the air inlet pipe 31 for being connected to light hydrogen cracking tank 1, air inlet
The end of pipe 31 is provided with blast pipe 32 on 1 bottom wall of light hydrogen cracking tank, air blower 3, and air mistake is provided in blast pipe 32
Filter core 321.It is provided with barometric pipe 4 outside light hydrogen cracking tank 1,4 one end of barometric pipe is connected to light hydrogen cracking tank 1 and another
One end is connected to air inlet pipe 31, is provided on barometric pipe 4 and flows into air inlet pipe 31 for controlling the gas in light hydrogen cracking tank 1
Interior check valve 41.
As shown in Figure 2 and Figure 3, air inlet pipe 31 runs through close to the position of 1 roof of light hydrogen cracking tank mounting hole 311, mounting hole
It is rotatably connected to shaft 312 in 311, sealing bearing 5 is provided between 311 inner wall of 312 outer wall of shaft and mounting hole, seals bearing
5 include outer ring 51, inner ring 52, ball 53, and inner ring 52 is fixed on 312 outer wall of shaft, the interference fit of outer ring 51 in mounting hole 311
Wall, outer ring 51, inner ring 52 have been coated with insulated paint on ball 53（It is not shown in the figure）.Shaft 312 is located inside air inlet pipe 31
Side wall is provided with blade 313, one end outside air inlet pipe 31 is provided with fan 314.
When needing to prepare mixed empty lighter hydrocarbons, pass through the pump housing（It is not shown in the figure）By the liquid light hydrocarbon edge in lighter hydrocarbons storage tank 2
Connecting tube 21 be pumped in light hydrogen cracking tank 1, then hot water is passed through in heating tube 12, by heat exchange principle to heating tube
12 are heated, and the liquid light hydrocarbon heat in light hydrogen cracking tank 1 vaporizes to form steam state lighter hydrocarbons at this time.Then start air blower 3, drum
Extraneous air is pumped into blast pipe 32 by blower 3, after the filtering using air filtration core 321, by air along air inlet pipe
31 are blown into light hydrogen cracking tank 1, and air and steam state lighter hydrocarbons are mixed into empty lighter hydrocarbons at this time, then mix empty lighter hydrocarbons along exhaust pipe 11
Discharge, user or combustion apparatus are i.e. using mixed empty lighter hydrocarbons at this time.
When air blower 3 blows air into air inlet pipe 31, the impact force impact blade 313 of air is moved, at this time blade 313
Shaft 312 is driven to rotate, inner ring 52 of the shaft 312 with dynamic bearing is rotated along ball 53, and shaft 312 drives fan 314 to rotate,
Air and steam state lighter hydrocarbons are uniformly mixed using the active force that the rotation of fan 314 generates, and then form uniformly mixed mixed sky
Lighter hydrocarbons.And when blowing air into air inlet pipe 31, the air in light hydrogen cracking tank 1 is along barometric pipe 4 and check valve
41 flow into air inlet pipe 31, keep light hydrogen cracking tank 1 and the air pressure in the external world to be in equilibrium-like always using barometric pipe 4
State, when avoiding that pressure is excessive in light hydrogen cracking tank 1, the liquid light hydrocarbon of 1 bottom of light hydrogen cracking tank is forced out.
As shown in Fig. 2, the lower end of light hydrogen cracking tank 1 is provided with sewage pipe 13, valve 14 is provided on sewage pipe 13.Lighter hydrocarbons
1 lower end of reactor tank is provided with stabilizer blade 15, and the detector 16 for detecting the flammable Gas content in air is provided on stabilizer blade 15.
A little impurity can be generated after lighter hydrocarbons vaporization in light hydrogen cracking tank 1, after excessive impurities accumulation, opens valve 14,
Impurity can be discharged by the sewage pipe 13 of 1 lower end of light hydrogen cracking tank, after impurity is removed, turn off valve 14.It is logical
The flammable Gas content in the setting detection air of detector 16 is crossed, when content is exceeded, alarm warning worker can occur for detector 16,
Avoid flammable Gas content is exceeded from exploding.
Working principle：When the mixed empty lighter hydrocarbons of preparation, pass through the pump housing（It is not shown in the figure）Liquid in lighter hydrocarbons storage tank 2 is light
Hydrocarbon is pumped in light hydrogen cracking tank 1, and then hot water is passed through in heating tube 12, the liquid light hydrocarbon heat vapour in light hydrogen cracking tank 1
Change forms steam state lighter hydrocarbons.Start air blower 3, extraneous air is blown into light hydrogen cracking tank 1 by air blower 3, at this time air and vapour
State lighter hydrocarbons are mixed into empty lighter hydrocarbons.When air blower 3 blows air into air inlet pipe 31, the impact force of air blows the fortune of blade 313
Dynamic, blade 313 drives shaft 312 and fan 314 to rotate, and air and steam state lighter hydrocarbons is uniformly mixed, and then form mixing
Uniform mixed empty lighter hydrocarbons.
Specific embodiment is only the explanation to the utility model, is not limitations of the present invention, this field
Technical staff can according to need the modification that not creative contribution is made to the present embodiment after reading this specification, but only
It will be in the scope of the claims of the utility model all by the protection of Patent Law.
Claims (8)
1. a kind of preparation facilities of mixed empty light-hydrocarbon gas, it is characterised in that：Including light hydrogen cracking tank (1), lighter hydrocarbons storage tank (2),
Air blower (3), the lighter hydrocarbons storage tank (2) is equipped with the connecting tube (21) for being connected to light hydrogen cracking tank (1) lower end, described
Light hydrogen cracking tank (1) upper end is equipped with exhaust pipe (11), and middle part is equipped in the light hydrogen cracking tank (1) and is located at the light hydrogen cracking tank
(1) internal and both ends are located at the external heating tube of the light hydrogen cracking tank (1) after being fed through light hydrogen cracking tank (1) side wall
(12), the air blower (3) is equipped with the air inlet pipe (31) for being connected to the light hydrogen cracking tank (1), the air inlet pipe (31)
End is close to light hydrogen cracking tank (1) bottom wall.
2. a kind of preparation facilities of mixed empty light-hydrocarbon gas according to claim 1, it is characterised in that：The air inlet pipe (31)
Position close to light hydrogen cracking tank (1) roof is rotatably connected in the mounting hole (311) through having mounting hole (311)
Shaft (312), the shaft (312) be located at the internal side wall of the air inlet pipe (31) be provided with blade (313), be located at it is described into
The external one end of tracheae (31) is provided with fan (314).
3. a kind of preparation facilities of mixed empty light-hydrocarbon gas according to claim 2, it is characterised in that：The shaft (312)
Sealing bearing (5) is provided between outer wall and the mounting hole (311) inner wall, the sealing bearing (5) includes outer ring (51), interior
(52), ball (53) are enclosed, the inner ring (52) is fixed on the shaft (312) outer wall, outer ring (51) interference fit and institute
State mounting hole (311) inner wall.
4. a kind of preparation facilities of mixed empty light-hydrocarbon gas according to claim 3, it is characterised in that：The outer ring (51),
The inner ring (52), the ball have been coated with insulated paint on (53).
5. a kind of preparation facilities of mixed empty light-hydrocarbon gas according to claim 1, it is characterised in that：The light hydrogen cracking tank
(1) external to be provided with barometric pipe (4), described barometric pipe (4) one end is connected to the light hydrogen cracking tank (1) and another
End is connected to the air inlet pipe (31), is provided on the barometric pipe (4) for controlling in the light hydrogen cracking tank (1)
Gas flows into the check valve (41) in the air inlet pipe (31).
6. a kind of preparation facilities of mixed empty light-hydrocarbon gas according to claim 1, it is characterised in that：The air blower (3)
On be provided with blast pipe (32), is provided with air filtration core (321) in the blast pipe (32).
7. a kind of preparation facilities of mixed empty light-hydrocarbon gas according to claim 1, it is characterised in that：The light hydrogen cracking tank
(1) lower end is provided with sewage pipe (13), is provided with valve (14) on the sewage pipe (13).
8. a kind of preparation facilities of mixed empty light-hydrocarbon gas according to claim 1, it is characterised in that：The light hydrogen cracking tank
(1) lower end surface is provided with stabilizer blade (15), and the detection for detecting the flammable Gas content in air is provided on the stabilizer blade (15)
Instrument (16).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820314994.8U CN208124347U (en) | 2018-03-07 | 2018-03-07 | A kind of preparation facilities of mixed empty light-hydrocarbon gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820314994.8U CN208124347U (en) | 2018-03-07 | 2018-03-07 | A kind of preparation facilities of mixed empty light-hydrocarbon gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208124347U true CN208124347U (en) | 2018-11-20 |
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ID=64205342
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820314994.8U Active CN208124347U (en) | 2018-03-07 | 2018-03-07 | A kind of preparation facilities of mixed empty light-hydrocarbon gas |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113058451A (en) * | 2021-04-09 | 2021-07-02 | 沈阳信元瑞科技有限公司 | Gas making tank |
| CN114931914A (en) * | 2022-06-02 | 2022-08-23 | 安徽省谱诺药化设备有限公司 | Sealed feeding and discharging type stainless steel reaction kettle and feeding and discharging method thereof |
-
2018
- 2018-03-07 CN CN201820314994.8U patent/CN208124347U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113058451A (en) * | 2021-04-09 | 2021-07-02 | 沈阳信元瑞科技有限公司 | Gas making tank |
| CN113058451B (en) * | 2021-04-09 | 2023-04-18 | 沈阳清能环保科技有限公司 | Gas making tank |
| CN114931914A (en) * | 2022-06-02 | 2022-08-23 | 安徽省谱诺药化设备有限公司 | Sealed feeding and discharging type stainless steel reaction kettle and feeding and discharging method thereof |
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