CN206504352U - A kind of light-hydrocarbon gas converting apparatus - Google Patents
A kind of light-hydrocarbon gas converting apparatus Download PDFInfo
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- CN206504352U CN206504352U CN201621187477.6U CN201621187477U CN206504352U CN 206504352 U CN206504352 U CN 206504352U CN 201621187477 U CN201621187477 U CN 201621187477U CN 206504352 U CN206504352 U CN 206504352U
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- light
- converting apparatus
- hydrocarbon gas
- transmitter
- heat transfer
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Abstract
A kind of light-hydrocarbon gas converting apparatus, including vaporization reaction stove, air compressor, fuel delivery device and heater, gasification reacting furnace includes housing, enclosure interior is additionally provided with the stable intensifier of honeycomb cellular type bubbler, heat transfer device and oil gas, the honeycomb cellular type bubbler is connected with air intake, the heat transfer device is arranged on below honeycomb cellular type bubbler, and the stable intensifier of the oil gas is arranged on above honeycomb cellular type bubbler, and the heater is connected with heat transfer device；The effective area that the light-hydrocarbon gas converting apparatus can steep raw material system is maximized, and makes bubble evenly, improves gas making efficiency.
Description
Technical field
The utility model is related to a kind of equipment that vaporise liquid hydrocarbons are changed into combustion gas, more particularly to a kind of light
The fuel gas reforming equipment of hydrocarbon.
Background technology
Light-hydrocarbon gas, is, using the byproduct in oil, natural gas extraction and process as gas raw material processed, to be fired by lighter hydrocarbons
Gas generating means, using physic vaporization mode, is converted into gaseous air mixture by liquid light hydrocarbon, is pipelined to terminal
User.Light-hydrocarbon gas is clean fuel as natural gas, all.In addition to calorific value is high, burning and exhausting is cleaned, with natural gas and liquid
Liquefied oil gas is compared, and it transports, stored, distributing more convenient safety, can be used as resident's diet, bathing, heating etc. various
The source of the gas of life gas facility, is also the industry such as the public utilities such as office, school, restaurant and glass, ceramics, building materials, food
Enterprise's culinary art, heating, refrigeration and the preferable source of the gas for producing heating facility.Country is for encouraging and facilitating the lighter hydrocarbons energy within 2010
National standard has been formulated in development.
Existing light-hydrocarbon gas converting apparatus is mainly gasification furnace, be compressed, vibrated by the lighter hydrocarbons to liquid, temperature
The light hydrocarbon gas that the modes such as change, filtering are produced, flammable light-hydrocarbon gas is mixed to form with compressed air.Such as Application No.
201610241669.9 Chinese patent disclose a kind of duct type light carbon gasifier, including：Mixed blank pipe, hot blast variable pump,
Petroleum pipeline, oil plant variable pump and programmable controller；The air intake of mixed blank pipe is provided with air intake check valve, and outlet side is provided with combustion
Gas outgassing nonreturn valve, air intake check valve is connected with hot blast variable pump；Cyclone is sequentially installed with mixed blank pipe from top to bottom, is prevented
Electrostatic net, pressure sensor and thermocouple；Offer oil transportation tube inlet on the body of mixed blank pipe, the port of export of petroleum pipeline passes through defeated
Oil pipe entrance is stretched into mixed blank pipe, and petroleum pipeline, which is stretched on the tube wall of part, offers some oil plant outlets, the arrival end of petroleum pipeline
Oil transportation check valve is connected with, oil transportation check valve is connected with oil plant variable pump；Programmable controller respectively with hot blast variable pump, oil plant
Variable pump, pressure sensor and thermocouple are electrically connected with.Although the light carbon gasifier can realize preferable light hydrocarbon effect
Really, but its gasification pipe for vibration, temperature become control problem and cause fuel gas reforming efficiency not maximize, indirectly waste
The energy, while supply gas pressure is unstable, mixed empty proportioning is not good, causes the combustion gas thermal efficiency caused that can not fully burn to decline,
Connect and cause secondary exhaust emission.And be directly entered by hot blast inside oil, there is the combustion gas after vaporization and inversely return and thermocouple
Contact and there is potential safety hazard.In addition, automaticity is low, causing labour to waste and be also easy to produce safe hidden artificial interference composition more
Suffer from.
The content of the invention
In order to solve the above-mentioned technical problem, the purpose of this utility model is to provide a kind of light-hydrocarbon gas converting apparatus, should
The effective area that light-hydrocarbon gas converting apparatus can steep raw material system is maximized, and makes bubble evenly, improves gas making efficiency.
The utility model is achieved through the following technical solutions：
A kind of light-hydrocarbon gas converting apparatus, including vaporization reaction stove, air compressor, fuel delivery device and heater, vapour
Changing reacting furnace includes housing, and housing side is provided with air intake and charging aperture from top to bottom, and the top of housing is provided with combustion gas
Outlet, air compressor is connected with air intake, and fuel delivery device is connected with charging aperture, and enclosure interior is additionally provided with honeycomb
The stable intensifier of formula bubbler, heat transfer device and oil gas, the honeycomb cellular type bubbler is connected with air intake, the heat transfer device
It is arranged on below honeycomb cellular type bubbler, the stable intensifier of the oil gas is arranged on above honeycomb cellular type bubbler, the heating
Device is connected with heat transfer device.
It is preferred that, the honeycomb cellular type bubbler includes being provided with the middle part of hollow discoidal housing, housing top surface
Air inlet, the top surface of housing is additionally provided with several ventholes, and venthole is centered around around air inlet and circular array point
Cloth.
It is preferred that, the outlet opening is regular hexagon, is also covered with venthole and hollow is shaped as going out for positive six terrace with edge
A point stomata is provided with gas hood, the side of air leaving cover, on the side of the air leaving cover of the setting at point stomata interval.
It is preferred that, the stable intensifier of the oil gas is made up of the stacking of multilayer honeycomb boards.
It is preferred that, the heat transfer device is the parallel coiled heat transfer device of multiple row.
It is preferred that, the air compressor is multisection type turbine air compressor reducer.
It is preferred that, the heater includes being provided with heating element heater in thermostat, heat transfer pump, the thermostat, heat
Liquid in thermostat is delivered in heat transfer device by conduction pump by pipeline.
It is preferred that, it is additionally provided with pressure stability groove between the air compressor and air intlet.
It is preferred that, the light-hydrocarbon gas converting apparatus also includes intelligence control system, and the intelligence control system includes electricity
Source master control, PLC and expansion module, frequency converter, pressure gauge, the first fluid level transmitter, magnetic double level gauge, first pressure pick-up
Device, second pressure transmitter, the first temperature transmitter, second temperature transmitter and control panel, the frequency converter, the first liquid level
Transmitter, first pressure transmitter, second pressure transmitter, the first temperature transmitter, second temperature transmitter, control panel lead to
Terminal is crossed with PLC and expansion module to even；The first pressure transmitter is arranged on pressure stability groove；The vaporization reaction stove
Top is provided with pressure gauge and second pressure transmitter, and side is provided with magnetic double level gauge and the first fluid level transmitter, side
The first temperature transmitter is provided with the middle part of side；Thermostat is provided with second temperature transmitter；The frequency converter and air compressor phase
Connection.
Advantage in the utility model compared with prior art is：
1st, the honeycomb cellular type bubbler and oil gas of a kind of light-hydrocarbon gas converting apparatus that the utility model is provided are stable strengthens
The lantern ring type that device is used can sufficiently realize that the effective area of raw material system bubble is maximized, and accurate honeycomb cellular type distribution makes system bubble more
Uniformly, by accurately calculating between the oil gas stabilizer of multilayer honeycomb boards, it is to avoid flow-disturbing and make system steep efficiency reduction.
2nd, the thermostat and heat transfer device for a kind of light-hydrocarbon gas converting apparatus that the utility model is provided are to even forming independent
Heating system, heats heat-conducting medium, it is ensured that the security of heating system using cluster type tubular electrothermal element.
3. a kind of parallel coiled heat transfer device of multiple row for light-hydrocarbon gas converting apparatus that the utility model is provided causes raw material
It is heated evenly, is conducive to improving gas making efficiency.
4. a kind of multisection type turbine air compressor reducer for light-hydrocarbon gas converting apparatus that the utility model is provided is adapted to respectively
Plant pressure demand, it is ensured that the stability of pressure.
Brief description of the drawings
Fig. 1 is the schematic diagram of light-hydrocarbon gas converting apparatus.
Fig. 2 is the schematic diagram of honeycomb cellular type bubbler.
Fig. 3 is the schematic diagram of the air leaving cover in honeycomb cellular type bubbler.
Fig. 4 is the top view of the stable intensifier of oil gas.
Fig. 5 is the front view of the stable intensifier of oil gas.
Fig. 6 is the schematic diagram of the parallel coiled heat transfer device of multiple row.
Fig. 7 is the schematic diagram of intelligence control system control panel.
Embodiment
It is new to this practicality below in conjunction with accompanying drawing to make the purpose of this utility model, technical scheme and advantage clearer
Type is described in further detail.
As shown in figure 1, a kind of light-hydrocarbon gas converting apparatus, including vaporization reaction stove 10, air compressor 20, fuel delivery device
30 and heater 40, gasification reacting furnace 10 includes housing 12, and the bottom of housing is provided with air intake 14 and entered from top to down
Material mouth 16, the top of housing is provided with gas outlet 18, and air compressor 20 is connected with air intake 14, fuel delivery device 30 with
Charging aperture 16 is connected, and the stable intensifier 70 of honeycomb cellular type bubbler 50, heat transfer device 60 and oil gas is additionally provided with inside housing 12,
The honeycomb cellular type bubbler 50 is connected with air intake 14, and the heat transfer device 60 is arranged under honeycomb cellular type bubbler 50
Side, the stable intensifier 70 of the oil gas is arranged on the top of honeycomb cellular type bubbler 50, the heater 40 and heat transfer device 60
It is connected.With reference to Fig. 1, fuel delivery device 30 includes oil storage tank 32 and oil pump 34, and oil pump 34 is by the lighter hydrocarbons of the liquid in oil storage tank 32
It is delivered in vaporization reaction stove 10.Air is transported in honeycomb cellular type bubbler by air compressor 20 by air intake 14,
Honeycomb cellular type bubbler is immersed in the lighter hydrocarbons of liquid, and air constantly overflows from bubbler processed, and heat transfer device 60 is constantly right
The lighter hydrocarbons of liquid in vaporization reaction stove 10 are heated, and vaporize the lighter hydrocarbons of liquid, thus the air overflowed in bubbler processed and
The lighter hydrocarbons of gasification are constantly mixed, and are then sent out from fuel outlet 18.
As shown in Figures 2 and 3, the honeycomb cellular type bubbler 50 includes hollow discoidal housing 52, housing top surface
Middle part be provided with air inlet 54, the top surface of housing is additionally provided with several ventholes 56, and venthole is centered around around air inlet
And circular array is distributed.As shown in Figures 2 and 3, outlet opening 56 is also to be covered with hollow shape on regular hexagon, venthole
Shape is to be provided with point stomata 59 on the air leaving cover 58 of positive six terrace with edge, the side of air leaving cover, the air leaving cover of the setting at point stomata interval
Side on.The air entered in the housing of honeycomb cellular type bubbler 50 comes out from venthole 56, is kept off by the top surface of air leaving cover 58
After firmly from each point of stomata 59 of air leaving cover it is inner it is scattered out can effectively increase the effective area of system bubble, improve system bubble
Efficiency.
As shown in Figure 4 and Figure 5, the stable intensifier 60 of the oil gas is made up of the stacking of multilayer honeycomb boards 62, every layer of honeycomb boards
On be all uniformly provided with several honeycombs 64, the number of plies of the stable intensifier of oil gas according to demand depending on, Fig. 3 show for three
Layer, but this is not limited to, it is connected between two adjacent honeycomb boards by connecting pole 66.
As shown in fig. 6, the heat transfer device 60 is the parallel coiled heat transfer device of multiple row, the parallel coiled heat transfer device energy of the multiple row
Enough make raw material heated evenly, be conducive to improving gas making efficiency.It is further preferred that air compressor is multisection type turbine air
Compressor reducer, the multisection type turbine air compressor reducer adapts to various pressure demands, it is ensured that the stability of pressure.The air compression
Pressure stability groove 22, the gas that pressure stability groove can come out to air compressor 20 are additionally provided between device 20 and air intlet
Cached and pressurize, the further stability for ensureing to enter the inner air pressure of gasification reacting furnace 10.
With reference to Fig. 1 and Fig. 6, the heater bag 40 is included to be provided with thermostat 42, heat transfer pump 44, the thermostat
Liquid in thermostat is delivered in heat transfer device by heating element heater 46, heat transfer pump by pipeline, can be used in thermostat 42
Water-bath or oil bath, the water or oil then passed to by heat after being heated in pump the last 44 thermostat are delivered in heat transfer device, are increased
The stability of the temperature of heat transfer device.
With reference to Fig. 1 and Fig. 7, the light-hydrocarbon gas converting apparatus also includes intelligence control system, the intelligence control system
Including power supply master control 80, PLC81, expansion module 82, frequency converter 83, pressure gauge 84, the first fluid level transmitter 85, panel processed 86,
Magnetic double level gauge 87, first pressure transmitter 88, second pressure transmitter 89, the first temperature transmitter 90 and second temperature become
Send device 91, the frequency converter, the first fluid level transmitter, first pressure transmitter, second pressure transmitter, the first temperature pick-up
Device, second temperature transmitter, control panel are by terminal and PLC and expansion module to even；The first pressure transmitter is set
On pressure stability groove；Pressure gauge and second pressure transmitter are provided with the top of the gasification reacting furnace, side is provided with magnetic and turned over
Plate liquid level gauge and the first fluid level transmitter, middle side edge are provided with the first temperature transmitter；Thermostat becomes provided with second temperature
Send device；The frequency converter is connected with air compressor.Change intelligence control system can monitor at any time the light-hydrocarbon gas conversion set
Standby temperature and pressure, and can voluntarily adjust its temperature and pressure, it is easy to use, but also can carry out manually and
Automatically switching, safer when using, and can tackle some special circumstances.
Above disclosed is only the utility model preferred embodiment, can not limit the utility model with this certainly
Interest field, therefore equivalent variations made according to the utility model claim still belong to the scope that the utility model is covered.
Claims (9)
1. a kind of light-hydrocarbon gas converting apparatus, including vaporization reaction stove, air compressor, fuel delivery device and heater, vaporization
Reacting furnace includes housing, and housing side is provided with air intake and charging aperture from top to bottom, and the top of housing is provided with combustion gas and gone out
Mouthful, air compressor is connected with air intake, and fuel delivery device is connected with charging aperture, it is characterised in that enclosure interior is also set
The stable intensifier of honeycomb cellular type bubbler, heat transfer device and oil gas is equipped with, the honeycomb cellular type bubbler is connected with air intake,
The heat transfer device is arranged on below honeycomb cellular type bubbler, and the stable intensifier of the oil gas is arranged in honeycomb cellular type bubbler
Side, the heater is connected with heat transfer device.
2. a kind of light-hydrocarbon gas converting apparatus according to claim 1, it is characterised in that the honeycomb cellular type bubbler bag
Include and air inlet is provided with the middle part of hollow discoidal housing, housing top surface, the top surface of housing is additionally provided with several outlets
Hole, venthole is centered around around air inlet and circular array is distributed.
3. a kind of light-hydrocarbon gas converting apparatus according to claim 2, it is characterised in that the outlet opening is positive six side
Also it is covered with shape, venthole on the hollow air leaving cover for being shaped as positive six terrace with edge, the side of air leaving cover and is provided with a point stomata, point
On the side of the air leaving cover of the setting at stomata interval.
4. a kind of light-hydrocarbon gas converting apparatus according to claim 3, it is characterised in that the stable intensifier of the oil gas by
The stacking of multilayer honeycomb boards is constituted.
5. a kind of light-hydrocarbon gas converting apparatus according to claim 4, it is characterised in that the heat transfer device is led for coiled
Hot device.
6. a kind of light-hydrocarbon gas converting apparatus according to claim 5, it is characterised in that the air compressor is multistage
Formula turbine air compressor reducer.
7. a kind of light-hydrocarbon gas converting apparatus described in claim 6, it is characterised in that the heater include thermostat,
Heating element heater is provided with heat transfer pump, the thermostat, the liquid in thermostat is delivered to and led by heat transfer pump by pipeline
In hot device.
8. a kind of light-hydrocarbon gas converting apparatus according to claim 7, it is characterised in that the air compressor and air
Pressure stability groove is additionally provided between import.
9. a kind of light-hydrocarbon gas converting apparatus according to claim 8, it is characterised in that the light-hydrocarbon gas converting apparatus
Also include intelligence control system, the intelligence control system include power supply master control, PLC and expansion module, frequency converter, pressure gauge,
First fluid level transmitter, magnetic double level gauge, first pressure transmitter, second pressure transmitter, the first temperature transmitter, second
Temperature transmitter and control panel, the frequency converter, the first fluid level transmitter, first pressure transmitter, second pressure transmitter,
First temperature transmitter, second temperature transmitter, control panel are by terminal and PLC and expansion module to even；First pressure
Power transmitter is arranged on pressure stability groove；The vaporization reaction furnace roof portion is provided with pressure gauge and second pressure transmitter, side
While being provided with magnetic double level gauge and the first fluid level transmitter, middle side edge is provided with the first temperature transmitter；Set on thermostat
There is second temperature transmitter；The frequency converter is connected with air compressor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621187477.6U CN206504352U (en) | 2016-10-28 | 2016-10-28 | A kind of light-hydrocarbon gas converting apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621187477.6U CN206504352U (en) | 2016-10-28 | 2016-10-28 | A kind of light-hydrocarbon gas converting apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206504352U true CN206504352U (en) | 2017-09-19 |
Family
ID=59843626
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621187477.6U Expired - Fee Related CN206504352U (en) | 2016-10-28 | 2016-10-28 | A kind of light-hydrocarbon gas converting apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206504352U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109945225A (en) * | 2019-03-13 | 2019-06-28 | 张梅 | Combustion gas generation device |
| CN111473357A (en) * | 2020-05-14 | 2020-07-31 | 山东省晟轩热能科技有限公司 | Hydrocarbon gas air feeder |
-
2016
- 2016-10-28 CN CN201621187477.6U patent/CN206504352U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109945225A (en) * | 2019-03-13 | 2019-06-28 | 张梅 | Combustion gas generation device |
| CN111473357A (en) * | 2020-05-14 | 2020-07-31 | 山东省晟轩热能科技有限公司 | Hydrocarbon gas air feeder |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170919 Termination date: 20191028 |