CN209702682U - A kind of single-pot multicomponent light-hydrocarbon gas generation device - Google Patents
A kind of single-pot multicomponent light-hydrocarbon gas generation device Download PDFInfo
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- CN209702682U CN209702682U CN201920548277.6U CN201920548277U CN209702682U CN 209702682 U CN209702682 U CN 209702682U CN 201920548277 U CN201920548277 U CN 201920548277U CN 209702682 U CN209702682 U CN 209702682U
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Abstract
The utility model discloses a kind of single-pot multicomponent light-hydrocarbon gas generation device, the single-pot multicomponent light-hydrocarbon gas generation device, the reactor tank is equipped with oil inlet and gas outlet；The heating unit that material is heated；The temperature conditioning unit being connected with heating unit, for controlling the heating temperature of the heating unit；Bubbling unit in reactor tank；The air compression unit being connected with bubbling unit is additionally provided with moisture trap between air compression unit and bubbling unit；The unit that is bubbled includes that first in reactor tank is bubbled disk and the second bubbling disk, first bubbling disk and the second bubbling disk pass through the first air inlet pipe and the second air inlet pipe is connected with the output end of gas compression unit respectively, the caliber of the caliber of first air inlet pipe greater than second air inlet pipe.The single-pot multicomponent light-hydrocarbon gas generation device, realizes the gasification of a variety of heterogeneity oil plants, and apparatus structure is simple, safety is good, and construction cost is more cheap.
Description
Technical field
The utility model relates to a kind of single-pot multicomponent light-hydrocarbon gas generation devices.
Background technique
Petrochemical Enterprises meeting a large amount of lighter hydrocarbons of by-product in light crude oil pretreatment, the coal that country advocates, which cleans, utilizes coal system
Also a large amount of stable light hydrocarbons of by-product, safe and effective utilize of this part lighter hydrocarbons have important value during oil.
Currently, being to be passed through gasification for the processing mode of light crude oil by-product lighter hydrocarbons and coal oil by-product stable light hydrocarbon
Processing equipment gasification is that fuel gas uses, and traditional processing equipment generally includes gas heating tank, knockout drum, gas and receives
Collect holding vessel etc., equipment is complex, and because lighter hydrocarbons flash-point is also lower than gasoline flash-point, highly volatile, and equipment connection is lengthy and jumbled
It is then easy to cause safety accident, risk is high.In addition, traditional gasification process equipment can only be to essence point (boiling range 25-60 in lighter hydrocarbons
C4-C5 component) isopentane feeds gasify, deal with objects it is more single, have some limitations.
Utility model content
The utility model provides the single-pot multicomponent lighter hydrocarbons combustion that a kind of structure is simple, equipment cost is low, safety is good
Gas generation device, solves problems of the prior art.
Used technical solution is the utility model to solve above-mentioned technical problem:
A kind of single-pot multicomponent light-hydrocarbon gas generation device, comprising:
Reactor tank, the reactor tank are equipped with oil inlet and gas outlet；
The heating unit that material is heated；
The temperature conditioning unit being connected with heating unit, for controlling the heating temperature of the heating unit；
Bubbling unit in reactor tank；
The air compression unit being connected with bubbling unit is additionally provided with air water between air compression unit and bubbling unit
Separator, the moisture in moisture compressed gas that carries for generating air compression unit gasification are separated, and water is avoided
Divide and enters the influence combustion gas generation of reactor tank internal water accumulation with compressed gas；
The unit that is bubbled includes that first in reactor tank is bubbled disk and the second bubbling disk, and described first is bubbled disk position
In the lower part that second is bubbled disk, the first bubbling disk and the second bubbling disk pass through the first air inlet pipe and the second air inlet pipe and gas respectively
The output end of compression unit is connected, and the caliber of first air inlet pipe is greater than the caliber of second air inlet pipe.In use, tool
There is the compressed air of certain pressure to enter bubbling disk by the first air inlet pipe or the second air inlet pipe, and passes through bubble holes point thereon
It dissipates and enters in oil plant, so that the oil plant with certain temperature is gasified, and transfer out reactor tank under compressed air pressure.Difference rule
The first air inlet pipe and the second air inlet pipe of lattice are suitable for the gasification of heterogeneity oil plant.
For example, when the oil plant being passed through in reactor tank is the by-product pentane of light crude oil, since its gasification temperature is lower,
Oil plant is heated to 14 degree or so by heating unit, while the warp of the compressed gas to reactor tank is passed through by air compressor
It is bubbled unit to blast into oil plant, oil plant gasification is made to generate required combustion gas of burning.It should be noted that it is higher in summer temperature,
Heating unit use can be disconnected.
When the oil plant being passed through in reactor tank is the by-product stable light hydrocarbon of coal oil, since its gasification temperature is higher, need
It wants heating unit that oil plant is heated to 30-35 degree or so, while being passed through the compressed gas to reactor tank by air compressor
It is bubbled unit to blast into oil plant, oil plant gasification is made to generate required combustion gas of burning.
The temperature of above-mentioned heating unit is controlled by temperature conditioning unit and is set.
Preferably, the heating unit includes the heating layer being coated on the outside of reactor tank, and glass can be used in the heating layer
Fiber heater band.
Preferably, the heating unit further includes a normally closed type temperature detect switch (TDS) (45 degree) being connected with heating layer, is so set
It sets, in temperature conditioning unit failure cisco unity malfunction, the normally closed type temperature detect switch (TDS) of setting is in heating unit heats to the upper limit
The power supply that heating heating unit can be cut off when temperature in time, avoids heating layer temperature from crossing high-risk.
Preferably, the temperature conditioning unit includes the temperature sensor being sequentially connected with the heating unit and temperature control
Device, temperature sensor are used to detect the heating layer temperature of heating unit, and controller controls required heating temperature for setting.
Preferably, first disk and the second bubbling disk are bubbled set on the lower part of reactor tank, convenient for making full use of in reactor tank
Oil plant can also increase bubbling and oil plant time of contact, guarantee gasification rate.
Preferably, the first bubbling disk includes a spherical shell, the first bubble holes is uniformly provided on spherical shell, bubble group aperture is
3mm。
Preferably, the second bubbling disk includes an endless tube, the second bubble holes is uniformly provided on endless tube, bubble group aperture is
3mm。
Preferably, the stomata of the endless tube is set to the middle and lower part or bottom of the endless tube, since stable light hydrocarbon includes light
Matter component and heavy component, wherein heavy component is easy deposition to reaction pot bottom, and endless tube is so set, can make heavy group
Point stress turns over, and increases the mixing between light components, and the gasification for being conducive to stable light hydrocarbon utilizes.
Preferably, liquidometer is equipped in reactor tank.
Preferably, intake valve is respectively equipped in first air inlet pipe and the second air inlet pipe.
Preferably, air outlet valve and pressure gauge are equipped on the escape pipe being connected with gas outlet.
Preferably, the air compression unit is air compressor machine.
Preferably, a support plate is additionally provided in the reactor tank, first air inlet pipe runs through the affixed support plate
Setting is also convenient for stability when the first air inlet pipe uses convenient for fixation of first air inlet pipe in reactor tank.
It is additionally provided with shield in the top of gas outlet, intake valve, air outlet valve etc., for dust-proof.
The utility model using the above structure, has the advantage that the single-pot multicomponent light-hydrocarbon gas generation device, leads to
Cross and different the first air inlet pipe and the second air inlet pipe of specification be set in single reaction tank, and respectively with the first air inlet pipe and the
The first bubbling disk and second that two air inlet pipe are connected is bubbled disk, realizes the gasification of a variety of heterogeneity oil plants, and apparatus structure
Simply, safety is good, and construction cost is more cheap, and cost cost is close to 1/10th of traditional cost.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model embodiment；
Fig. 2 is the schematic diagram that heating unit is connect with control unit in Fig. 1.
In figure, 1, reactor tank, 2, oil inlet, 3, gas outlet, 4, air compression unit, 5, first is bubbled disk, and 6, second is bubbled
Disk, the 7, first air inlet pipe, the 8, first intake valve, 9, moisture trap, 10 heating units, 11, intake valve, 12 air outlet valves, 13, pressure
Power table, 14, support plate, 15, control temperature unit；
101, power supply, 102, temp control switch, 103, heating layer, 104, relay；
1501, temperature controller, 1502, temperature sensor.
Specific embodiment:
In order to clarify the technical characteristics of the invention, below by specific embodiment, and its attached drawing is combined, to this reality
It is described in detail with novel.
In the description of the present application, it is to be understood that term " center ", "upper", "lower", "front", "rear", " left side ",
The orientation or position of the instructions such as " right side ", "vertical", "horizontal", "top", "bottom", "inner", "outside", " axial direction ", " radial direction ", " circumferential direction "
Relationship is to be based on the orientation or positional relationship shown in the drawings, and is merely for convenience of description the application and simplifies description, without referring to
Show or imply that signified device or element must have a particular orientation, be constructed and operated in a specific orientation, therefore cannot manage
Solution is the limitation to the application.
All the embodiments in this specification are described in a progressive manner, same and similar portion between each embodiment
Dividing may refer to each other, and each embodiment focuses on the differences from other embodiments.
In addition, term " first ", " second " are used for descriptive purposes only and cannot be understood as indicating or suggesting relative importance
Or implicitly indicate the quantity of indicated technical characteristic.Define " first " as a result, the feature of " second " can be expressed or
Implicitly include one or more of the features.In the description of the present application, the meaning of " plurality " is two or more,
Unless otherwise specifically defined.
In this application unless specifically defined or limited otherwise, term " installation ", " connected ", " connection ", " fixation " etc.
Term shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integral；It can be mechanical connect
It connects, is also possible to be electrically connected, can also be communication；It can be directly connected, can also indirectly connected through an intermediary, it can be with
It is the interaction relationship of the connection or two elements inside two elements.For the ordinary skill in the art, may be used
To understand the concrete meaning of above-mentioned term in this application as the case may be.
In this application unless specifically defined or limited otherwise, fisrt feature in the second feature " on " or " down " can be with
It is that the first and second features directly contact or the first and second features pass through intermediary mediate contact.In retouching for this specification
In stating, the description of reference term " one embodiment ", " some embodiments ", " example ", " specific example " or " some examples " etc.
Mean that particular features, structures, materials, or characteristics described in conjunction with this embodiment or example are contained at least one of the application
In embodiment or example.In the present specification, schematic expression of the above terms are necessarily directed to identical embodiment
Or example.Moreover, particular features, structures, materials, or characteristics described can be in any one or more of the embodiments or examples
It can be combined in any suitable manner.
As shown in fig. 1, in the present embodiment, the single-pot multicomponent light-hydrocarbon gas generation device, comprising:
Reactor tank 1 is equipped with oil inlet 2 and gas outlet 3 in reactor tank 1；The heating unit 10 that material is heated；With
The connected temperature conditioning unit 15 of heating unit 10, for controlling the heating temperature of the heating unit 10；Drum in reactor tank 1
Steep unit；The air compression unit 4 being connected with bubbling unit is additionally provided with air water between air compression unit and bubbling unit
Separator 9, the moisture in moisture compressed gas that carries for generating the gasification of air compression unit 4 are separated, are avoided
Moisture, which enters 1 internal water accumulation of reactor tank with compressed gas, influences combustion gas generation；
The unit that is bubbled includes that first in reactor tank 1 is bubbled disk 5 and the second bubbling disk 6, is produced by being bubbled disk
It is raw to be bubbled, it can promote oil plant gasification rate；Described first, which is bubbled disk 5, is located at the second lower part for being bubbled disk 6, and first is bubbled 5 He of disk
Second bubbling disk 6 is connected by the first air inlet pipe 7 and the second air inlet pipe 8 with the output end of gas compression unit 7 respectively, described
The caliber of first air inlet pipe 7 is greater than the caliber of second air inlet pipe 8.Before use, 1 being passed through by oil inlet 2 into reactor tank
Oil plant guarantees that oil plant can cover the first bubbling disk 5 and second and be bubbled disk 6.
In use, starting air compression unit 4, when the by-product pentane that the oil plant being passed through in reactor tank 1 is light crude oil
When, the gasification temperature as needed for gasifying pentane is lower, 10-14 DEG C of temperature energy steam raising with air pressure capable of being increased, when oil plant in reactor tank 1
When temperature deficiency sets gasification temperature, gasification temperature is made up to by heating unit heats, while air compression unit exports
Compressed air obtain the gas of temperature about 3-6 degree through the first air inlet pipe 7 after moisture trap 9 isolates moisture, and pass through
First bubbling disk 5 is bubbled into oil plant, and the gasifying pentane made forms fuel gas, is applied on combustor through gas outlet 3.
When the oil plant being passed through in reactor tank 1 is the by-product stable light hydrocarbon of coal oil, such as the gasification temperature of naphtha
About 30-35 degree or so, it is therefore desirable to which by the oil plant in heating unit heats reactor tank, while air compression unit 4 exports
Compressed air obtain the gas of temperature about 3-6 degree through the second air inlet pipe 8 after moisture trap 9 isolates moisture, and pass through
Second bubbling disk 6 is bubbled into oil plant, and the stable light hydrocarbon made gasifies to form fuel gas, is applied on combustor i.e. through gas outlet 3
It can.
Wherein the vapor pressure of pentane is at 0.5 kilogram, with stable light hydrocarbon vapor pressure at 0.7-1 kilograms.
Intelligible, the heating unit 10 is coated on the heating layer 103 on the outside of reactor tank, the heating layer 103
Glass fibre heating tape can be used.
It is intelligible, the heating unit 10 further include one be connected with heating layer 103 normally closed type temperature detect switch (TDS) 102 (on
Limiting temperature is 45 degree, i.e., when 1 temperature of reactor tank reaches 45 degree, the disconnection of normally closed type temperature detect switch (TDS) 102) and, by normally closed type when use
Temperature detect switch (TDS) is close to reactor tank 1 and is arranged, so set, in 15 failure cisco unity malfunction of temperature conditioning unit, setting it is normal
Enclosed temperature detect switch (TDS) 102 can cut off the power supply of heating heating unit 10 when heating unit 10 is heated to ceiling temperature in time,
103 temperature of heating layer is avoided to cross high-risk.
It is intelligible, the temperature conditioning unit 15 include the temperature sensor 1502 being sequentially connected with the heating unit 10 and
Temperature controller 1501, the temperature controller 1501 are connect with the relay 104 being connected with heating layer, the temperature sensor
1502, which are close to reactor tank 1, is arranged, and for detecting 1 temperature of reactor tank, 1 temperature of reactor tank for heating heating unit 10 is controlled in temperature
Spend 1501 set temperature of controller.
It is intelligible, in order to make full use of the oil plant in reaction tube, the first bubbling disk 5 and the second bubbling disk 6 can be set to
The lower part of reactor tank guarantees that being bubbled operation carries out.
Intelligible, when oil plant is pentane property oil plant, the tolerance requirement is lower, and first, which is bubbled disk 5, includes a ball
Shell is uniformly provided with the first bubble holes on spherical shell.So set, requirement can be met.
Intelligible, when oil plant is stable light hydrocarbon property oil plant, second, which is bubbled disk 6, includes an endless tube, on endless tube
It is even to offer the second bubble holes.And the stomata of the endless tube is set to the middle and lower part or bottom of the endless tube, mainly due to stabilization
Lighter hydrocarbons include light components and heavy component, and wherein heavy component is easy deposition to reaction pot bottom, so set, can make
Heavy component stress turns over, and increases the mixing between light components, and the gasification for being conducive to stable light hydrocarbon utilizes.
It is intelligible, in order to measure safe minimum liquid level, that is, the first minimum liquid level for being bubbled disk and the second bubbling disk is covered,
Liquidometer can be equipped in reactor tank 1.
It is intelligible, in order to control compressed air air mass flow, divide in first air inlet pipe 7 and the second air inlet pipe 8
It She You not intake valve 11.
It is intelligible, in order to control throughput and the pressure out of fuel gas, on the escape pipe being connected with gas outlet 3
Equipped with equipped with air outlet valve 12 and pressure gauge 13.
Intelligible, the air compression unit 4 is air compressor machine.
It is intelligible, a support plate 14 is additionally provided in the reactor tank 1, first air inlet pipe 7 is through affixed described
Support plate 14 is arranged, and convenient for fixation of first air inlet pipe 7 in reactor tank 1, is also convenient for firm when the first air inlet pipe 7 uses
Property.It is additionally provided with shield in the top of gas outlet, intake valve, air outlet valve etc., for dust-proof.
Above-mentioned specific embodiment cannot function as the limitation to scope of protection of the utility model, for the skill of the art
For art personnel, any alternate modification or transformation made to the utility model embodiment all fall within the guarantor of the utility model
It protects in range.
Place is not described in detail for the utility model, is the well-known technique of those skilled in the art of the present technique.
Claims (10)
1. a kind of single-pot multicomponent light-hydrocarbon gas generation device characterized by comprising
Reactor tank, the reactor tank are equipped with oil inlet and gas outlet；
The heating unit that material is heated；
The temperature conditioning unit being connected with heating unit, for controlling the heating temperature of the heating unit；
Bubbling unit in reactor tank；
The air compression unit being connected with bubbling unit is additionally provided with gas-water separation between air compression unit and bubbling unit
Device；
The unit that is bubbled includes that first in the reactor tank is bubbled disk and second and is bubbled disk, and described first, which is bubbled disk, is located at the
Two are bubbled the lower part of disk, and the first bubbling disk and the second bubbling disk pass through the first air inlet pipe and the second air inlet pipe and gas compression respectively
The output end of unit is connected, and the caliber of first air inlet pipe is greater than the caliber of second air inlet pipe.
2. a kind of single-pot multicomponent light-hydrocarbon gas generation device according to claim 1, which is characterized in that the heating
Unit includes the heating layer being coated on the outside of reactor tank, and the heating layer uses glass fibre heating tape.
3. a kind of single-pot multicomponent light-hydrocarbon gas generation device according to claim 2, which is characterized in that the heating
Unit further includes a normally closed type temperature detect switch (TDS) being connected with heating layer.
4. a kind of single-pot multicomponent light-hydrocarbon gas generation device according to claim 1, which is characterized in that the temperature control
Unit includes the temperature sensor and temperature controller being sequentially connected with the heating unit.
5. a kind of single-pot multicomponent light-hydrocarbon gas generation device according to claim 1, which is characterized in that first is bubbled
Disk and second is bubbled the lower part that disk is set to reactor tank.
6. a kind of single-pot multicomponent light-hydrocarbon gas generation device according to claim 1, which is characterized in that first is bubbled
Disk includes a spherical shell, and the first bubble holes are uniformly provided on spherical shell.
7. a kind of single-pot multicomponent light-hydrocarbon gas generation device according to claim 1, which is characterized in that second is bubbled
Disk includes an endless tube, and the second bubble holes are uniformly provided on endless tube.
8. a kind of single-pot multicomponent light-hydrocarbon gas generation device according to claim 7, which is characterized in that the endless tube
Stomata be set to the middle and lower part or bottom of the endless tube.
9. a kind of single-pot multicomponent light-hydrocarbon gas generation device according to claim 1, which is characterized in that described first
Intake valve is respectively equipped in air inlet pipe and the second air inlet pipe.
10. a kind of single-pot multicomponent light-hydrocarbon gas generation device according to claim 1, which is characterized in that with go out
The escape pipe that port is connected is equipped with air outlet valve and pressure gauge.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920548277.6U CN209702682U (en) | 2019-04-22 | 2019-04-22 | A kind of single-pot multicomponent light-hydrocarbon gas generation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920548277.6U CN209702682U (en) | 2019-04-22 | 2019-04-22 | A kind of single-pot multicomponent light-hydrocarbon gas generation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209702682U true CN209702682U (en) | 2019-11-29 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920548277.6U Active CN209702682U (en) | 2019-04-22 | 2019-04-22 | A kind of single-pot multicomponent light-hydrocarbon gas generation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209702682U (en) |
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2019
- 2019-04-22 CN CN201920548277.6U patent/CN209702682U/en active Active
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