CN207094186U - A kind of blending transport of hydrogen gas natural gas and separator - Google Patents
A kind of blending transport of hydrogen gas natural gas and separator Download PDFInfo
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- CN207094186U CN207094186U CN201721096198.3U CN201721096198U CN207094186U CN 207094186 U CN207094186 U CN 207094186U CN 201721096198 U CN201721096198 U CN 201721096198U CN 207094186 U CN207094186 U CN 207094186U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P90/00—Enabling technologies with a potential contribution to greenhouse gas [GHG] emissions mitigation
- Y02P90/45—Hydrogen technologies in production processes
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Abstract
Blending transport and separator the utility model discloses a kind of hydrogen gas natural gas, including for conveying the transfer pipeline of material, transfer pipeline is provided with Hydrogen Energy input port and the mixing device for Hydrogen Energy and material to be blended；The transfer pipeline other end is additionally provided with isolates and purifies device for separate Hydrogen Energy, isolates and purifies and Hydrogen Energy delivery outlet is provided with device.The blending transport of hydrogen gas natural gas provided herein and separator are transformed the transfer pipeline of existing material, by adding Hydrogen Energy input port and Hydrogen Energy delivery outlet and in input and output procedure by being blended and being separated Hydrogen Energy and material, the conveying to realizing Hydrogen Energy is realized.The utility model realizes the Hydrogen Energy transport of a large amount of efficient stables using existing Location Detection of Medium Transportation Pipeline, it is possible to achieve most economical Hydrogen Energy means of transportation, is the necessary support that the Hydrogen Energy application of urban area provides.
Description
Technical field
Energy technical field of transportation is the utility model is related to, the blending more specifically to a kind of hydrogen gas natural gas is transported
Defeated and separator.
Background technology
Chinese hydrogen annual production has exceeded ten million ton of scale, occupies the first in the world.Plant-scale hydrogen production process mainly includes
Fossil energy hydrogen manufacturing such as methane steam reforming and two methods of utilization clean energy resource electric power water electrolysis hydrogen production, wherein fossil energy are such as
Coal chemical industry and methane reforming hydrogen manufacturing account for 96%, and the yield of water electrolysis hydrogen production accounts for world's hydrogen total output 3%, also have many industry
A large amount of hydrogen, which are produced, in production process such as chlor-alkali and methanol production process accounts for 1% as byproduct.Although fossil energy hydrogen manufacturing
It is hydrogen production process most economical at present, but it not only consumes a large amount of fossil fuels in process of production, and produce a large amount of dioxies
Change carbon.
In the application end of Hydrogen Energy, the fuel cell car using Hydrogen Energy is can uniquely to reach automotive performance index comprehensively
Environmentally friendly vehicle, maximum social effect are that instead of the Battery disposal and pollution problem of oil and conventional lithium battery automobile, hydrogen fuel electricity
The advantages of pond automobile, is really a lot, but so far also without scale of mass production hydrogen cell automobile appearance.
Therefore for the manufacturing side of Hydrogen Energy, China be world wide Hydrogen Energy yield maximum country, following Hydrogen Energy industry
Development key be Hydrogen Energy transport and efficient application.And either liquid hydrogen low-temperature transport or high pressure tank body transports at present,
This ultralow temperature and high-pressure process can all cause specific energy resource consumption.And the large-scale fuel cell technology for power generation and hydrogen of application end
Gas fuel engine power generation technology is also transported by hydrogen and inexpensively stable hydrogen source is very few is influenceed, at present slower development.
In summary, how a kind of stabilization and cheap hydrogen transportation resources are provided, be current those skilled in the art urgently
The problem of to be solved.
Utility model content
In view of this, the purpose of this utility model is to provide blending transport and the separator of a kind of hydrogen gas natural gas, should
Device can ensure that the course of conveying of Hydrogen Energy is convenient and stably.
To achieve these goals, the utility model provides following technical scheme：
A kind of blending transport of hydrogen gas natural gas and separator, it is characterised in that including the conveying for conveying material
Pipeline, the transfer pipeline are provided with Hydrogen Energy input port and the mixing device for Hydrogen Energy and the material to be blended；
The transfer pipeline other end is additionally provided with isolates and purifies device for separate Hydrogen Energy, described to isolate and purify
Hydrogen Energy delivery outlet is provided with device.
Preferably, flow monitoring device and the flow control for being used for monitoring Hydrogen Energy flow value are provided with the Hydrogen Energy input port
Device processed, the flow monitoring device are connected with the mixing device, and the mixing device is controlled by the Hydrogen Energy flow value
The volume control device.
Preferably, the material inlet of the mixing device and the Hydrogen Energy input port are provided with the pressure for being used for measuring inlet pressure
Power table；And/or the material outlet for isolating and purifying device and the Hydrogen Energy delivery outlet are provided with the pressure for being used for measuring outlet pressure
Power table.
Preferably, the pressure gauge is connected with control device, when the pressure that the pressure gauge measures exceeds preset value, institute
Control device is stated to control the mixing device to be stopped and close the Hydrogen Energy input port.
Preferably, the material is gas material, and the mixing device is to be mixed what gas material and hydrogen were blended
Mixing device, the device that isolates and purifies is to isolate and purify device by what hydrogen separated with gas material.
Preferably, the gas material is natural gas.
Preferably, the mixing device is to realize that hydrogen fills with the blending that gas material blends by changing stream pressure
Put, the Hydrogen Vapor Pressure in the hydrogen inlet of the mixing device is more than the pressure of the material of material inlet port.
Preferably, the mixing device includes axial flow blower mixed flow mixing device and emanated in air ejector mixing device extremely
Few one kind.
Preferably, the device that isolates and purifies includes cryogenic separation device, pressure-swing absorption apparatus, membrane separation device and joint
At least one of industrial separation device.
Preferably, the transfer pipeline is crude oil pipeline or product pipeline, and the mixing device is by hydrogen
Gas is mixed into the mixing device in crude oil or product oil, and the device that isolates and purifies is point by hydrogen by being separated in mixture
From purification devices.
Material provided by the utility model can be liquid material or gas material, and above-mentioned transfer pipeline can be selected more
The transfer pipeline of the existing material of kind.
In the application, Hydrogen Energy input port and Hydrogen Energy delivery outlet are set on conveying circuit, and relatively, Hydrogen Energy input port is located at
It is located on transfer pipeline closer to the position of material input, Hydrogen Energy delivery outlet on transfer pipeline closer to material delivery outlet
Position.That is, Hydrogen Energy can enter transfer pipeline by Hydrogen Energy input port, and along the conveying side of material on transfer pipeline
To moving, finally transfer pipeline is discharged in Hydrogen Energy delivery outlet.
During Hydrogen Energy inlet and outlet transfer pipeline, it is required to handle Hydrogen Energy and material.Set in Hydrogen Energy input port
The mixing device that Hydrogen Energy and material are blended, the separation that Hydrogen Energy and material are isolated and purified is set in Hydrogen Energy delivery outlet
Purification devices.
The blending transport of hydrogen gas natural gas provided herein and separator enter to the transfer pipeline of existing material
Row transformation, by adding Hydrogen Energy input port and Hydrogen Energy delivery outlet and in input and output procedure by the way that Hydrogen Energy and material are entered
Row blending and separation, realize the conveying to realizing Hydrogen Energy.The utility model is realized a large amount of high using existing Location Detection of Medium Transportation Pipeline
The Hydrogen Energy transport of effect, it is possible to achieve most economical Hydrogen Energy means of transportation, be the necessary branch that the Hydrogen Energy application of urban area provides
Hold.
Brief description of the drawings
, below will be to embodiment in order to illustrate more clearly of the utility model embodiment or technical scheme of the prior art
Or the required accompanying drawing used is briefly described in description of the prior art, it should be apparent that, drawings in the following description are only
It is embodiment of the present utility model, for those of ordinary skill in the art, on the premise of not paying creative work, also
Other accompanying drawings can be obtained according to the accompanying drawing of offer.
Fig. 1 is the blending transport and the structural representation of separator of a kind of hydrogen gas natural gas provided by the utility model
Figure.
In Fig. 1：
1 it is material input, 11 be Hydrogen Energy input port, 12 is mixing device；
2 it is material delivery outlet, 21 is Hydrogen Energy delivery outlet, 22 to isolate and purify device；
31 it is the first air gauge, 32 be the second air gauge, 33 be the 3rd air gauge, 34 be the 4th air gauge, 35 is the 5th
Air gauge, 36 the 6th air gauges, 4 are transfer pipeline.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the embodiment of the utility model is carried out
Clearly and completely describing, it is clear that described embodiment is only the utility model part of the embodiment, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment obtained, belong to the scope of the utility model protection.
Core of the present utility model is to provide blending transport and the separator of a kind of hydrogen gas natural gas, and the device can be protected
The course of conveying for demonstrate,proving Hydrogen Energy is convenient and stably.
Fig. 1 is refer to, Fig. 1 is blending transport and the separator of a kind of hydrogen gas natural gas provided by the utility model
Structural representation.
A kind of blending transport of hydrogen gas natural gas provided by the utility model and separator, including for conveying material
Transfer pipeline 4, transfer pipeline 4 is provided with Hydrogen Energy input port 11 and the mixing device for Hydrogen Energy and material to be blended
12；The other end of transfer pipeline 4 is additionally provided with isolates and purifies device 22 for separate Hydrogen Energy, isolates and purifies on device 22
It is provided with Hydrogen Energy delivery outlet 21.
It should be noted that material can be liquid material or gas material, above-mentioned transfer pipeline 4 can be selected a variety of
The transfer pipeline of existing material, such as natural gas transportation pipeline, Crude Oil Transportation pipeline etc..Wherein, in natural gas transportation pipeline
Material be natural gas, the material in Crude Oil Transportation pipeline is crude oil or product oil etc..
The material input 1 and material delivery outlet 2 of material, material input 1 and material are usually provided with transfer pipeline
It is conveying circuit between delivery outlet 2, material is by course of conveying that the process of material input 1 to material delivery outlet 2 is material.
In the application, Hydrogen Energy input port 11 and Hydrogen Energy delivery outlet 21 are set on conveying circuit, and relatively, Hydrogen Energy input port 11 is located at defeated
Send is located at defeated closer to material on transfer pipeline 4 on pipeline 4 closer to the position of material input 1, Hydrogen Energy delivery outlet 21
The position of outlet 2.That is, Hydrogen Energy can enter transfer pipeline 4 by Hydrogen Energy input port 11, and along thing on transfer pipeline 4
The conveying direction of material moves, and finally discharges transfer pipeline 4 in Hydrogen Energy delivery outlet 21.
Need, it is to be noted that during Hydrogen Energy inlet and outlet transfer pipeline 4, to be required to handle Hydrogen Energy and material.Tool
Body, the mixing device 12 that Hydrogen Energy and material are blended is set in Hydrogen Energy input port 11, and being set in Hydrogen Energy delivery outlet 21 will
Hydrogen Energy isolates and purifies device 22 with what material was isolated and purified.The two can use Hydrogen Energy ripe in the prior art to mix
Mixed, purifying plant.
Hydrogen Energy provided in the application can include liquified hydrogen and Gaseous Hydrogen etc..
The blending transport of hydrogen gas natural gas provided herein and separator enter to the transfer pipeline of existing material
Row transformation, by adding Hydrogen Energy input port 11 and Hydrogen Energy delivery outlet 21 and in input and output procedure by by Hydrogen Energy and thing
Material is blended and separated, and realizes the conveying to realizing Hydrogen Energy.The utility model is realized big using existing Location Detection of Medium Transportation Pipeline
Measure efficient Hydrogen Energy transport, it is possible to achieve most economical Hydrogen Energy means of transportation, be necessity that the Hydrogen Energy application of urban area provides
Support.
In order to lift the safe to use of hydrogen energy source and ensure that blending procedure meets standard requirement, on the basis of above-described embodiment
On, the flow monitoring device and volume control device for being used for monitoring Hydrogen Energy flow value, flow are provided with Hydrogen Energy input port 11
Monitoring device is connected with mixing device 12, and mixing device 12 controls volume control device by Hydrogen Energy flow value.
It should be noted that it can be each that above-mentioned flow monitoring device, which can be device, the volume control devices such as flowmeter,
The valve body of type, switch or other there is the device of switching capacity.
When Hydrogen Energy is Gaseous Hydrogen, above-mentioned flow monitoring device can be gas flowmeter, gas meter etc.；Hydrogen Energy is liquid
When, flow monitoring device is fluid inspection valve etc..
In the present embodiment, Hydrogen Energy flow value is obtained by flow monitoring device, and Hydrogen Energy flow value is sent to blending dress
12 are put, judges whether to need to adjust volume control device by mixing device 12.When Hydrogen Energy flow value exceeds preset value, flow control
Flow is turned down or closed by device processed.
On the basis of any one above-mentioned embodiment, the material inlet of mixing device 12 and Hydrogen Energy input port 11 are provided with
For measuring the pressure gauge of inlet pressure；And/or isolate and purify device 22 material outlet and Hydrogen Energy delivery outlet 21 be provided be used for
Measure the pressure gauge of outlet pressure.
It should be noted that above-mentioned pressure gauge can be used for and mixing device or isolates and purifies device and be connected respectively, so as to
Monitoring mixing device or isolate and purify device inlet and outlet pressure, avoid the occurrence of air pressure or the excessive situation of hydraulic pressure.
On the basis of above-described embodiment, pressure gauge is connected with control device, when the pressure that pressure gauge measures is beyond pre-
If during value, control device controls mixing device 12 to be stopped and closes Hydrogen Energy input port 11.
It should be noted that because the course of conveying of transfer pipeline 4 needs to be monitored flow and pressure, it is defeated to avoid
Send in pipeline 4 and the excessive or too low situation of air pressure occur.
On the basis of any one above-mentioned embodiment, Hydrogen Energy can be specially hydrogen, and material can be specially gas
Material, mixing device 12 are the mixing device 12 for being blended gas material and hydrogen, and it is by hydrogen to isolate and purify device 22
What is separated with gas material isolates and purifies device 22.
Alternatively, gas material is natural gas.Alternatively, above-mentioned gas material can also be the material of other forms.
On the basis of above-described embodiment, mixing device is to realize that hydrogen is mixed with gas material by changing stream pressure
Mixed mixing device 12, the Hydrogen Vapor Pressure in the hydrogen inlet of mixing device 12 are more than the pressure of the material of material inlet port.
Specifically, mixing device 12 can select transformation mixing device common in the art, and mixing device 12 includes
Axial flow blower mixed flow mixing device and at least one of air ejector mixing device of emanating.
It should be noted that it can be carried out simultaneously using several different types of mixing device in blending procedure, i.e., simultaneously
Connection uses, naturally it is also possible to carries out several different types of mixing device successively, that is, is used in series.
On the basis of any one above-mentioned embodiment, isolating and purifying device includes cryogenic separation device, pressure-variable adsorption
At least one of device, membrane separation device and joint industrial separation device.
The use of above-mentioned mixing device 12, which can be equally extrapolated to, to be isolated and purified on device, and isolating and purifying device equally can be with
Realized and combined by least two serial or parallel connection, here is omitted.
In any one above-mentioned embodiment, Fig. 1 is refer to, wherein, it is provided with the material inlet position of mixing device 12
For the first air gauge 31 of the air pressure for measuring gas material, it is provided with the hydrogen inlet position of mixing device 12 and is used to measure hydrogen
Second air gauge 32 of the air pressure of gas, the gas for being used for measuring mixed gas is provided with the mixed gas outlet position of mixing device 12
3rd air gauge 33 of pressure.
The 4th gas of the air pressure for being used to measure mixed gas is provided with the mixed gas entry position for isolating and purifying device 22
Table 34 is pressed, the air gauge 35 of air pressure the 5th for being used for measuring hydrogen is provided with the position for isolating and purifying the hydrogen gas outlet of device 22,
The 6th air gauge 36 of the air pressure for being used to measure natural gas is provided with the natural gas delivery outlet position for isolating and purifying device 22.
On the basis of any one above-mentioned embodiment, Hydrogen Energy is liquified hydrogen or Gaseous Hydrogen, and transfer pipeline 4 is that crude oil is defeated
Pipeline or product pipeline are sent, and mixing device 12 is the mixing device 12 hydrogen being mixed into crude oil or product oil, is separated
Purification devices 22 are that hydrogen is isolated and purified into device 22 by what is separated in mixture.
Blending transport and the primary structure of separator except the hydrogen gas natural gas provided in above-mentioned each embodiment,
The structure of other each several parts of the device refer to prior art, repeat no more herein.
Each embodiment is described by the way of progressive in this specification, what each embodiment stressed be and other
The difference of embodiment, between each embodiment identical similar portion mutually referring to.
The blending transport to hydrogen gas natural gas provided by the utility model and separator are described in detail above.
Specific case used herein is set forth to principle of the present utility model and embodiment, and the explanation of above example is only
It is to be used to help understand method and its core concept of the present utility model.It should be pointed out that the ordinary skill for the art
For personnel, on the premise of the utility model principle is not departed from, some improvement and modification can also be carried out to the utility model,
These are improved and modification is also fallen into the protection domain of the utility model claims.
Claims (10)
1. a kind of blending transport of hydrogen gas natural gas and separator, it is characterised in that including the delivery pipe for conveying material
Road (4), the transfer pipeline (4) are provided with Hydrogen Energy input port (11) and the blending for Hydrogen Energy and the material to be blended
Device (12)；
Transfer pipeline (4) other end is additionally provided with isolates and purifies device (22), the separation for separate Hydrogen Energy
Hydrogen Energy delivery outlet (21) is provided with purification devices (22).
2. the blending transport of hydrogen gas natural gas according to claim 1 and separator, it is characterised in that the Hydrogen Energy is defeated
Entrance (11) place is provided with the flow monitoring device and volume control device for being used for monitoring Hydrogen Energy flow value, the flow monitoring dress
Put and be connected with the mixing device (12), the mixing device (12) controls the flow control dress by the Hydrogen Energy flow value
Put.
3. the blending transport of hydrogen gas natural gas according to claim 2 and separator, it is characterised in that the blending dress
The material inlet and the Hydrogen Energy input port (11) for putting (12) are provided with the pressure gauge for being used for measuring inlet pressure；And/or described point
Material outlet and the Hydrogen Energy delivery outlet (21) from purification devices (22) are provided with and are used to measure the pressure gauge of outlet pressure.
4. the blending transport of hydrogen gas natural gas according to claim 3 and separator, it is characterised in that the pressure gauge
It is connected with control device, when the pressure that the pressure gauge measures exceeds preset value, the control device control blending dress
(12) are put to be stopped and close the Hydrogen Energy input port (11).
5. blending transport and the separator of the hydrogen gas natural gas according to any one of Claims 1-4, it is characterised in that
The material is gas material, and the mixing device (12) is the mixing device (12) for being blended gas material and hydrogen,
The device (22) that isolates and purifies is to isolate and purify device (22) by what hydrogen separated with gas material.
6. the blending transport of hydrogen gas natural gas according to claim 5 and separator, it is characterised in that the gas thing
Expect for natural gas.
7. the blending transport of hydrogen gas natural gas according to claim 5 and separator, it is characterised in that the blending dress
It is set to and realizes hydrogen and the mixing device (12) of gas material blending, the hydrogen of the mixing device (12) by changing stream pressure
Hydrogen Vapor Pressure in gas air inlet is more than the pressure of the material of material inlet port.
8. the blending transport of hydrogen gas natural gas according to claim 7 and separator, it is characterised in that the blending dress
Putting (12) includes axial flow blower mixed flow mixing device and at least one of air ejector mixing device of emanating.
9. the blending transport of hydrogen gas natural gas according to claim 5 and separator, it is characterised in that the separation is pure
Makeup is put including at least one of cryogenic separation device, pressure-swing absorption apparatus, membrane separation device and joint industrial separation device.
10. blending transport and the separator of the hydrogen gas natural gas according to any one of Claims 1-4, it is characterised in that
The transfer pipeline (4) is crude oil pipeline or product pipeline, and the mixing device (12) is that hydrogen is mixed into original
Mixing device (12) in oil or product oil, the device (22) that isolates and purifies is point by hydrogen by being separated in mixture
From purification devices (22).
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721096198.3U CN207094186U (en) | 2017-08-29 | 2017-08-29 | A kind of blending transport of hydrogen gas natural gas and separator |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721096198.3U CN207094186U (en) | 2017-08-29 | 2017-08-29 | A kind of blending transport of hydrogen gas natural gas and separator |
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| CN207094186U true CN207094186U (en) | 2018-03-13 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107314242A (en) * | 2017-08-29 | 2017-11-03 | 赫普科技发展（北京）有限公司 | A kind of blending transport of hydrogen gas natural gas and separator |
| DE112020000096T5 (en) | 2019-08-07 | 2021-08-05 | Oleksandr Oleksandrovych Riepkin | Process for the formation and use of an energetic system with the integration of hydrogen, which has been generated using renewable energy sources, into the system |
-
2017
- 2017-08-29 CN CN201721096198.3U patent/CN207094186U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107314242A (en) * | 2017-08-29 | 2017-11-03 | 赫普科技发展（北京）有限公司 | A kind of blending transport of hydrogen gas natural gas and separator |
| DE112020000096T5 (en) | 2019-08-07 | 2021-08-05 | Oleksandr Oleksandrovych Riepkin | Process for the formation and use of an energetic system with the integration of hydrogen, which has been generated using renewable energy sources, into the system |
| DE202020005978U1 (en) | 2019-08-07 | 2024-02-06 | Oleksandr Oleksandrovych Riepkin | Energy system with hydrogen produced using renewable energy sources integrated into the system |
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