CN208123900U - A kind of independently supplying system of light-hydrocarbon gas - Google Patents
A kind of independently supplying system of light-hydrocarbon gas Download PDFInfo
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- CN208123900U CN208123900U CN201820315428.9U CN201820315428U CN208123900U CN 208123900 U CN208123900 U CN 208123900U CN 201820315428 U CN201820315428 U CN 201820315428U CN 208123900 U CN208123900 U CN 208123900U
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- lighter hydrocarbons
- gasifying pot
- steam boiler
- room
- light
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Abstract
The utility model discloses a kind of independently supplying systems of light-hydrocarbon gas, including steam boiler, closed room, lighter hydrocarbons gasifying pot is provided in room, the lower end of lighter hydrocarbons gasifying pot is wound with heating tape, room is externally provided with lighter hydrocarbons storage tank, lighter hydrocarbons storage tank lower end is equipped with the inlet tube of connection lighter hydrocarbons gasifying pot, lighter hydrocarbons gasifying pot is equipped with the delivery pipe for being connected to steam boiler, hollow heater box is provided in room, heater box lower end is equipped with the air inlet pipe of connection steam boiler, upper end is equipped with the muffler of connection steam boiler.The utility model has the following advantages that and effect：Lighter hydrocarbons gasifying pot is heated heating tape, so that liquid light hydrocarbon heat is vaporized into steam state lighter hydrocarbons, steam state lighter hydrocarbons are delivered in steam boiler along delivery pipe, steam boiler inner cold water is heated to generating steam by Light hydrocarbon burner, again by some vapor to heater box continuous heating, the temperature in room is improved, lighter hydrocarbons gasifying pot is heated indirectly, achieved the effect that facilitate lighter hydrocarbons vaporization, improved boil-off rate.
Description
Technical field
The utility model relates to new energy to supply field, in particular to the independently supplying system of a kind of 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.
For above-mentioned light hydrocarbon gas preparing device when manufacturing gaseous light hydrocarbons, the compression that liquid light hydrocarbon is generated by air compressor is empty
Air pressure goes out liquid light hydrocarbon tank, using after automatically controlled liquid pressure regulator valve with compressed air in atomizer can and, liquid light hydrocarbon quilt
Compressed air atomization is atomized in sliding and gasifying pot in heat exchange, then the fast vaporizing in heat exchange atomization, gasifying pot.Lighter hydrocarbons vaporized
Journey very complicated, and equipment investment is more, and cost is larger, has much room for improvement.
Utility model content
The purpose of the utility model is to provide a kind of independently supplying systems of light-hydrocarbon gas, have the effect for facilitating lighter hydrocarbons to vaporize
Fruit.
The above-mentioned technical purpose of the utility model technical scheme is that：A kind of light-hydrocarbon gas it is only
Vertical supply system is provided with lighter hydrocarbons gasifying pot, the lighter hydrocarbons gasifying pot including steam boiler, closed room in the room
Lower end outer wall be wound with heating tape, be provided with lighter hydrocarbons storage tank outside the room, lighter hydrocarbons storage tank lower end is equipped with connection
Inlet tube in lighter hydrocarbons gasifying pot upper end, the lighter hydrocarbons gasifying pot are equipped with the delivery pipe for being connected to the steam boiler,
Hollow heater box is provided in the room, the heater box lower end is equipped with the air inlet pipe for being connected to the steam boiler, institute
It states heater box upper end and is equipped with the muffler for being connected to the steam boiler.
Liquid by using above-mentioned technical proposal, when needing to generate steam using steam boiler, in lighter hydrocarbons storage tank
Lighter hydrocarbons flow into lighter hydrocarbons gasifying pot along inlet tube, then by the heating band connection power supply of lighter hydrocarbons gasifying pot lower end, heating tape pair
Lighter hydrocarbons gasifying pot is heated.Become steam state lighter hydrocarbons after the liquid light hydrocarbon heat vaporization in lighter hydrocarbons gasifying pot at this time, then steam state
Lighter hydrocarbons are delivered in steam boiler along delivery pipe, then light lighter hydrocarbons, the heat that Light hydrocarbon burner generates is in steam boiler
Cold water is heated, until cold water boiling generates steam, steam discharge is used for factory.When steam boiler generates steam,
Some vapor flows into heater box along air inlet pipe, then flows back in steam boiler further along muffler.The heat of steam at this time
Continuous heating is carried out to heater box, the heat of heater box is distributed along heating box outer wall to room, using distributing to room
Heat improve the temperature in room, and then lighter hydrocarbons gasifying pot is heated indirectly, has reached and facilitated lighter hydrocarbons vaporization, improve vapour
Change the effect of rate.
The utility model is further arranged to：It is provided in the delivery pipe for controlling in the lighter hydrocarbons gasifying pot
Lighter hydrocarbons flow into the check valve in the steam boiler.
By using above-mentioned technical proposal, make lighter hydrocarbons that can only flow into steam along lighter hydrocarbons gasifying pot by the way that check valve is arranged
In boiler, avoids the lighter hydrocarbons in steam boiler from flowing back and cause explosion.
The utility model is further arranged to：The inlet tube is provided with regulating valve.
By using above-mentioned technical proposal, it can control the flow velocity of lighter hydrocarbons by the way that regulating valve is arranged, avoid lighter hydrocarbons flow velocity mistake
Influence the normal feed of steam boiler slowly fastly or excessively.
The utility model is further arranged to：The lower end of the lighter hydrocarbons gasifying pot is provided with sewage pipe.
By using above-mentioned technical proposal, a little impurity can be generated after the lighter hydrocarbons vaporization in lighter hydrocarbons gasifying pot, when excessive miscellaneous
After matter accumulation, impurity can be discharged by the sewage pipe of lighter hydrocarbons gasifying pot lower end.
The utility model is further arranged to：The heater box lower end is provided with drain valve.
By using above-mentioned technical proposal, when inside the heated case of steam stream, some vapor is liquefied as in heater box
Water droplet, when a large amount of water droplets savings is behind heater box inside, opening drain valve the water in heater box is discharged, when water is completely exhausted out
Afterwards, drain valve is turned off.
The utility model is further arranged to：The heating box outer wall is provided with multiple cooling fins.
By using above-mentioned technical proposal, the radiating efficiency of heater box is improved by the way that cooling fin is arranged, and then increases heat
The utilization rate of amount, has only lacked thermal losses.
The utility model is further arranged to：It is provided in the room for detecting the flammable Gas content in air
Detector.
By using above-mentioned technical proposal, by the flammable Gas content in setting detector test air, when content is exceeded
When, detector occurs alarm and warns worker, avoids in room that flammable Gas content is exceeded to explode.
The utility model is further arranged to：The lower end surface of the lighter hydrocarbons gasifying pot is provided with stabilizer blade, on the stabilizer blade
It is provided with the bolt for fixing the lighter hydrocarbons gasifying pot.
By using above-mentioned technical proposal, lighter hydrocarbons gasifying pot is fixed by setting stabilizer blade and bolt, improves lighter hydrocarbons
The stability of gasifying pot, when the liquid light hydrocarbon in lighter hydrocarbons storage tank being avoided to flow into lighter hydrocarbons gasifying pot, lighter hydrocarbons gasifying pot shakes
It moves or topples over.
In conclusion the utility model has the advantages that：When generating steam using steam boiler, lighter hydrocarbons storage
Liquid light hydrocarbon in tank flows into lighter hydrocarbons gasifying pot along inlet tube, is heated using heating tape to lighter hydrocarbons gasifying pot, so that
Become steam state lighter hydrocarbons after the vaporization of liquid light hydrocarbon heat, then steam state lighter hydrocarbons are delivered to the combustion chamber of steam boiler along delivery pipe
It is interior, the cold water in steam boiler is heated using Light hydrocarbon burner.When steam boiler generate steam when, some vapor along into
Tracheae flows into heater box, then flows back in steam boiler further along muffler.The heat of steam holds heater box at this time
Continuous heating, the heat of heater box is distributed to the temperature in room in raising room, and then is heated indirectly to lighter hydrocarbons gasifying pot,
Accelerate the boil-off rate of lighter hydrocarbons.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of embodiment；
Fig. 2 is the structural schematic diagram of the lighter hydrocarbons gasifying pot of embodiment, heater box；
Fig. 3 is partial enlarged view at A in Fig. 2.
In figure：1, steam boiler；2, room；3, lighter hydrocarbons gasifying pot；31, stabilizer blade；32, bolt；33, heating tape；34, blowdown
Pipe；35, delivery pipe；36, check valve；4, lighter hydrocarbons storage tank；41, inlet tube；42, regulating valve；5, heater box；51, cooling fin；
52, drain valve；53, air inlet pipe；54, muffler；6, detector.
Specific embodiment
The utility model is described in further detail below in conjunction with attached drawing.
A kind of independently supplying system of light-hydrocarbon gas, as shown in Figure 1 and Figure 2, including steam boiler 1, closed room 2, room
Between be provided with lighter hydrocarbons gasifying pot 3 in 2, the lower end surface of lighter hydrocarbons gasifying pot 3 is provided with stabilizer blade 31, is provided on stabilizer blade 31 for fixing
The bolt 32 of lighter hydrocarbons gasifying pot 3；The lower end outer wall of lighter hydrocarbons gasifying pot 3 is wound with heating tape 33, the lower end setting of lighter hydrocarbons gasifying pot 3
There is sewage pipe 34.
As shown in Figure 1 and Figure 2, lighter hydrocarbons storage tank 4 is provided with outside room 2,4 lower end of lighter hydrocarbons storage tank is equipped with and is connected to lighter hydrocarbons
The inlet tube 41 of 3 upper end of gasifying pot, inlet tube 41 are provided with regulating valve 42.Lighter hydrocarbons gasifying pot 3 is equipped with and is connected to steam boiler 1
Delivery pipe 35, the check valve flowed into steam boiler 1 for controlling the lighter hydrocarbons in lighter hydrocarbons gasifying pot 3 is provided in delivery pipe 35
36（Referring to Fig. 3）.
As shown in Figure 2 and Figure 3, hollow heater box 5 is provided in room 2,5 outer wall of heater box is provided with multiple cooling fins
51,5 lower end of heater box is provided with drain valve 52, and 5 lower end of heater box is equipped with and is connected to steam boiler 1（Referring to Fig. 1）Air inlet pipe
53,5 upper end of heater box is equipped with the muffler 54 for being connected to steam boiler 1.
When needing to generate steam using steam boiler 1, first the regulating valve 42 on inlet tube 41 is opened, lighter hydrocarbons store up at this time
The liquid light hydrocarbon hidden in tank 4 flows into lighter hydrocarbons gasifying pot 3 along inlet tube 41, then by the heating tape of 3 lower end of lighter hydrocarbons gasifying pot
33 connection power supplys, lighter hydrocarbons gasifying pot 3 is heated in heating tape 33.Liquid light hydrocarbon heat vaporization in lighter hydrocarbons gasifying pot 3 at this time
After become steam state lighter hydrocarbons, then open delivery pipe 35 on check valve 36, steam state lighter hydrocarbons are delivered to steaming along delivery pipe 35 at this time
The combustion chamber of boiler furnace 1（It is not shown in the figure）It is interior, lighter hydrocarbons are then lighted, the heat that Light hydrocarbon burner generates is in steam boiler 1
Cold water is heated, until cold water boiling generates steam, steam discharge is used for factory.
When steam boiler 1 generate steam when, some vapor along air inlet pipe 53 flow into heater box 5 in, then further along return
Tracheae 54 flows back in steam boiler 1.The heat of steam carries out continuous heating to heater box 5 at this time, and the heat of heater box 5 is along adding
5 outer wall of hot tank and cooling fin 51 are distributed to room 2, using distribute in room 2 heat improve room 2 in temperature,
And then lighter hydrocarbons gasifying pot 3 is heated indirectly, and then accelerate the boil-off rate of lighter hydrocarbons.
After some vapor liquefies in heater box 5, drain valve 52 is opened at this time, water is discharged, after water is completely exhausted out,
Close drain valve 52.A little impurity can be generated after lighter hydrocarbons vaporization in lighter hydrocarbons gasifying pot 3, after excessive impurities accumulation, by light
Impurity is discharged the sewage pipe 34 of 3 lower end of hydrocarbon gasifying pot.
As shown in Fig. 2, being provided with the detector 6 for detecting the flammable Gas content in air in room 2.It is examined by setting
The flammable Gas content in the detection air of instrument 6 is surveyed, when content is exceeded, detector 6 occurs alarm and warns worker, avoids in room 2
Flammable Gas content is exceeded to explode.
Working principle：When generating steam using steam boiler 1, the liquid light hydrocarbon in lighter hydrocarbons storage tank 4 is along inlet tube
41 flow into lighter hydrocarbons gasifying pot 3, are heated using heating tape 33 to lighter hydrocarbons gasifying pot 3, so that after the vaporization of liquid light hydrocarbon heat
Become steam state lighter hydrocarbons, steam state lighter hydrocarbons are delivered in the combustion chamber of steam boiler 1 along delivery pipe 35 then, utilize Light hydrocarbon burner
Cold water in steam boiler 1 is heated.When steam boiler 1 generates steam, some vapor is flowed into along air inlet pipe 53 to be added
In hot tank 5, then flowed back in steam boiler 1 further along muffler 54.The heat of steam persistently add to heater box 5 at this time
Heat, the heat of heater box 5 is distributed to the temperature in room 2 in raising room 2, and then is heated indirectly to lighter hydrocarbons gasifying pot 3,
Accelerate the boil-off rate of 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 independently supplying system of light-hydrocarbon gas, it is characterised in that：Including steam boiler (1), closed room (2), institute
It states and is provided with lighter hydrocarbons gasifying pot (3) in room (2), the lower end outer wall of the lighter hydrocarbons gasifying pot (3) is wound with heating tape (33), institute
It states and is provided with lighter hydrocarbons storage tank (4) outside room (2), lighter hydrocarbons storage tank (4) lower end is equipped with and is connected to the lighter hydrocarbons gasifying pot
(3) inlet tube (41) of upper end, the lighter hydrocarbons gasifying pot (3) are equipped with the delivery pipe (35) for being connected to the steam boiler (1),
It is provided with hollow heater box (5) in the room (2), heater box (5) lower end is equipped with and is connected to the steam boiler (1)
Air inlet pipe (53), heater box (5) upper end, which is equipped with, is connected to the muffler (54) of the steam boiler (1).
2. a kind of independently supplying system of light-hydrocarbon gas according to claim 1, it is characterised in that：The delivery pipe (35)
On be provided with the check valve (36) flowed into the steam boiler (1) for controlling the lighter hydrocarbons in the lighter hydrocarbons gasifying pot (3).
3. a kind of independently supplying system of light-hydrocarbon gas according to claim 1, it is characterised in that：The inlet tube (41)
It is provided with regulating valve (42).
4. a kind of independently supplying system of light-hydrocarbon gas according to claim 1, it is characterised in that：The lighter hydrocarbons gasifying pot
(3) lower end is provided with sewage pipe (34).
5. a kind of independently supplying system of light-hydrocarbon gas according to claim 1, it is characterised in that：The heater box (5)
Lower end is provided with drain valve (52).
6. a kind of independently supplying system of light-hydrocarbon gas according to claim 1, it is characterised in that：The heater box (5)
Outer wall is provided with multiple cooling fins (51).
7. a kind of independently supplying system of light-hydrocarbon gas according to claim 1, it is characterised in that：In the room (2)
It is provided with the detector (6) for detecting the flammable Gas content in air.
8. a kind of independently supplying system of light-hydrocarbon gas according to claim 1, it is characterised in that：The lighter hydrocarbons gasifying pot
(3) lower end surface is provided with stabilizer blade (31), and the bolt for fixing the lighter hydrocarbons gasifying pot (3) is provided on the stabilizer blade (31)
(32)。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820315428.9U CN208123900U (en) | 2018-03-07 | 2018-03-07 | A kind of independently supplying system of light-hydrocarbon gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820315428.9U CN208123900U (en) | 2018-03-07 | 2018-03-07 | A kind of independently supplying system of light-hydrocarbon gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208123900U true CN208123900U (en) | 2018-11-20 |
Family
ID=64204329
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820315428.9U Active CN208123900U (en) | 2018-03-07 | 2018-03-07 | A kind of independently supplying system of light-hydrocarbon gas |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208123900U (en) |
-
2018
- 2018-03-07 CN CN201820315428.9U patent/CN208123900U/en active Active
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