CN208135896U - Skid-mounted type methanol and vapor plasma method reformation hydrogen production device of air - Google Patents
Skid-mounted type methanol and vapor plasma method reformation hydrogen production device of air Download PDFInfo
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- CN208135896U CN208135896U CN201820586157.0U CN201820586157U CN208135896U CN 208135896 U CN208135896 U CN 208135896U CN 201820586157 U CN201820586157 U CN 201820586157U CN 208135896 U CN208135896 U CN 208135896U
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- methanol
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- water storage
- output pipe
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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
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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Abstract
The utility model discloses a kind of skid-mounted type methanol and vapor plasma method reformation hydrogen production device of air comprising device noumenon, the device noumenon include：Methanol and water storage tank, with methanol and water storage tank intake line, methanol and water storage tank output pipe, between methanol and water storage tank intake line, methanol and water storage tank output pipe or methanol and water storage tank output pipe are equipped with metering pump；It is connected to the heat-conducting oil heating reaction kettle of methanol and water storage tank；It is connected to the vapour liquid separator of heat-conducting oil heating reaction kettle；It is connected to the plasma generator of vapour liquid separator；Plasma generator is connected to hydrogen gas combustor via check-valves and pressure reducing valve component.The utility model has the beneficial effects that：Device is skid-mounted type, small in size, convenient in carrying, and use is safe, and fuel cost cheaper than natural gas 20%, is a kind of energy-saving environmental protection device.
Description
Technical field
The utility model relates to petrochemical industries, more particularly, to a kind of skid-mounted type methanol and vapor plasma
Method reformation hydrogen production device of air.
Background technique
Hydrogen is one of current important energy source, the source of active development hydrogen.But, has the device by hydrogen from methyl alcohol, substantially
On be high temperature and pressure, yield is high, and cost of investment is high.
Utility model content
The purpose of this utility model be exactly to solve the above-mentioned problems, provide it is a kind of low cost, using the sled of safety economy
Dress formula methanol and vapor plasma method reformation hydrogen production device of air.
In order to solve the above technical problems, the utility model provides a kind of skid-mounted type methanol and vapor plasma method
Reformation hydrogen production device of air comprising device noumenon, the device noumenon include：Methanol and water storage tank, with methanol and water storage tank
Between intake line, methanol and water storage tank output pipe, methanol and water storage tank intake line, methanol and water storage tank output pipe or
Person's methanol and water storage tank output pipe are equipped with metering pump, methanol and water storage tank intake line, methanol and water storage tank output pipe
It is respectively arranged with control valve；It is connected to the heat-conducting oil heating reaction kettle of methanol and water storage tank；It is connected to heat-conducting oil heating reaction kettle
Vapour liquid separator；It is connected to the plasma generator of vapour liquid separator；Plasma generator is via check-valves and decompression
Valve module and be connected to hydrogen gas combustor.
Further, device noumenon is installed in container.
Further, methanol and water storage tank are made of corrosion resistant 304L stainless steel or Q345 steel plate, and in methanol and water storage tank
Top can arrange pressure relief opening.
The utility model has the advantages that：Device is skid-mounted type, small in size, convenient in carrying, and use is safe, fuel
Cost cheaper than natural gas 20%, is a kind of energy-saving environmental protection device.
Detailed description of the invention
Fig. 1 is skid-mounted type methanol and vapor plasma method reformation hydrogen production gas in the utility model first embodiment
Schematic device；
Fig. 2 is skid-mounted type methanol and vapor plasma method reformation hydrogen production gas in the utility model second embodiment
Schematic device.
Specific embodiment
In order to be easy to understand the technical means, creative features, achievement of purpose, and effectiveness of the utility model, under
In conjunction with specific embodiments, the utility model is further described in face.
The first embodiment of the utility model provides a kind of skid-mounted type methanol and vapor is reformed with plasma method
Hydrogen manufacturing device of air, as shown in Figure 1 comprising device noumenon, the device noumenon include：It is methanol and water storage tank 1, metering pump 2, thermally conductive
Oil heating reaction kettle 3, vapour liquid separator 4, plasma generator 5, check-valves and pressure reducing valve component 6, hydrogen gas combustor 7 and
Several conveying pipelines.
Referring to Fig. 1, methanol and water storage tank 1 install methanol and water storage tank intake line, methanol and water storage tank output pipe, first
Metering pump 2, methanol and water storage tank input pipe are installed between pure and mild water storage tank intake line, methanol and water storage tank output pipe
Road, methanol and water storage tank output pipe are disposed with control valve, in particular, in the input port and delivery outlet of methanol and water storage tank 1
Be respectively arranged with input port extension tube attached 81, delivery outlet extension tube attached 82, in input port extension tube attached by ring flange connect methanol and
Water storage tank intake line connects methanol and water storage tank output pipe by ring flange in delivery outlet extension tube attached, at this point, inputting
A control valve (not shown) is respectively set in mouth extension tube attached 81, delivery outlet extension tube attached 82, and in methanol and water storage tank input pipe
Road, methanol and water storage tank output pipe are also respectively arranged a control valve, i.e. intake line control valve 91, output pipe control respectively
Valve 92 processed, and an end of metering pump is connected to intake line control valve 91 and inputs the pipeline between control valve set by external pipeline 81
It is upper, another to be terminated at output pipe control valve 92 and export on the pipeline between control valve set by external pipeline 82, when needing first
Pure and mild water storage tank 1 supplements raw material, then can open control valve set by intake line control valve 91, input external pipeline 81 (at this time
Need to close control valve set by output pipe control valve 92, output external pipeline 82), and if necessary by methanol and water storage tank 1
Raw material be supplied to heat-conducting oil heating reaction kettle, at this point, then closing the set control of intake line control valve 91, output external pipeline 82
Valve processed opens simultaneously control valve and output pipe control valve 92 set by input external pipeline 81, at this point, raw material can be via defeated
Heat-conducting oil heating is delivered to after entering control valve, metering pump, output pipe control valve 92 set by external pipeline 81, input external pipeline
Reaction kettle.To complete to control the raw material supply stream that first alcohol and water is sent to heat-conducting oil heating reaction kettle through valve via metering pump
Journey.Methanol and water storage tank are made of corrosion resistant 304L stainless steel or Q345 steel plate.First alcohol and water is with volume fraction 1：1 mixing storage
It deposits, volume is generally 10-20m3.Metering pump is that a kind of pressure is 0.5Mpa, flow 5m3The chemical industry of/h is corrosion-resistant, resistance to 300 DEG C of temperature
Degree, the chemical pump of regulating flow quantity.
The heat-conducting oil heating reaction kettle 3 of methanol and water storage tank 1 is connected to by pipeline, heat-conducting oil heating reaction kettle 3
Intake line is connected with methanol and water storage tank output pipe, and the intake line of heat-conducting oil heating reaction kettle 3 is provided with control valve.
Heat-conducting oil heating reaction kettle is a kind of resistance to 300 DEG C of temperature, 2-5m3Drum type brake reaction kettle.
Vapor-liquid separation operation, vapour-liquid point are carried out by the vapour liquid separator 4 that pipeline is connected to heat-conducting oil heating reaction kettle 3
It is a kind of device that cooling liquid can be separated from device.
And it is connected in the plasma generator 5 of vapour liquid separator 4 and is equipped with cathode, anode discharge room.Plasma hair
Raw device is a kind of device of plasma obtained by artificial means.It is a kind of to make gas using extra electric field or high-frequency induction electric field
Conduction, also referred to as gas discharge.The high-temperature electric arc that plasma is generated by cathode and anode discharge, makes methanol and vapor moment
It is cracked into hydrogen and carbon monoxide, carbon dioxide.
Plasma generator is connected to hydrogen gas combustor (hydrogen via the pipeline for being equipped with check-valves and pressure reducing valve component 6
Gas burner special) 7.
The obtained hydrogen product of skid-mounted type methanol steam plasma method reforming hydrogen production device can be sent into hydrogen combustion
Burner is used as boiler, furnace fuel.
It is noted that device noumenon is mounted in 4 meters of long containers, moves and use.It is filled using the utility model
It sets with 1 kilogram of methanol and 1 kg of water, 2.7 cubes of hydrogen can be produced, calorific value is 8500 kilocalories.It is equivalent to 1 cube of natural gas
Calorific value.
The working principle of the utility model is：First alcohol and water is sent to heat-conducting oil heating reaction kettle via metering pump, is passed through
By gas-liquid separator, then via the anode and cathode arc chamber of plasma generator, enter via check-valves and pressure reducing valve, hydrogen is special
Boiler combustion is sent into burner.
Metering pump shown in FIG. 1 can directly open 1 front and back of methanol and water storage tank without its metering
Raw material can be supplied to follow-up equipment under external pressure by control valve, without that can only carry out according to principle above-mentioned
Work.
The second embodiment of the utility model provides a kind of skid-mounted type methanol and vapor is reformed with plasma method
Hydrogen manufacturing device of air is different from the first embodiment place and is, metering pump be directly installed on methanol and water storage tank 1 methanol and
On water storage tank output pipe.
Referring to fig. 2, the input port and delivery outlet of methanol and water storage tank 1 are respectively arranged with input port extension tube attached 81, delivery outlet
Extension tube attached 82, in input port, extension tube attached connects methanol and water storage tank intake line by ring flange, logical in delivery outlet extension tube attached
It crosses ring flange and connects methanol and water storage tank output pipe, methanol and water storage tank output pipe installation metering pump 2, and first alcohol and water
Storage tank intake line, methanol and water storage tank output pipe are generally in same horizontal line, methanol and water storage tank intake line,
Methanol and water storage tank output pipe are respectively disposed with control valve.
When needing to supply first alcohol and water to heat-conducting oil heating reaction kettle 3, then methanol and water storage tank output pipe 82 are opened
The first alcohol and water of methanol and water storage tank 1 can be transported to heat-conducting oil heating reaction kettle 3 at this time by control valve and metering pump 2.Afterwards
Continuous workflow can be found in first embodiment.
It will be understood by those skilled in the art that the respective embodiments described above are to realize the specific implementation of the utility model
Example, and in practical applications, can to it, various changes can be made in the form and details, without departing from the spirit of the utility model
And range.
Claims (3)
1. a kind of skid-mounted type methanol and vapor plasma method reformation hydrogen production device of air comprising device noumenon, feature
It is, which includes：
Methanol and water storage tank, with methanol and water storage tank intake line, methanol and water storage tank output pipe, methanol and water storage tank
Between intake line, methanol and water storage tank output pipe or methanol and water storage tank output pipe are equipped with metering pump, methanol and
Water storage tank intake line, methanol and water storage tank output pipe are respectively arranged with control valve；
It is connected to the heat-conducting oil heating reaction kettle of methanol and water storage tank；
It is connected to the vapour liquid separator of heat-conducting oil heating reaction kettle；
It is connected to the plasma generator of vapour liquid separator；
The plasma generator is connected to hydrogen gas combustor via check-valves and pressure reducing valve component.
2. skid-mounted type methanol according to claim 1 and vapor plasma method reformation hydrogen production device of air, feature
It is, described device ontology is installed in container.
3. skid-mounted type methanol according to claim 1 and vapor plasma method reformation hydrogen production device of air, feature
It is, the methanol and water storage tank are made of corrosion resistant 304L stainless steel or Q345 steel plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820586157.0U CN208135896U (en) | 2018-04-24 | 2018-04-24 | Skid-mounted type methanol and vapor plasma method reformation hydrogen production device of air |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820586157.0U CN208135896U (en) | 2018-04-24 | 2018-04-24 | Skid-mounted type methanol and vapor plasma method reformation hydrogen production device of air |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208135896U true CN208135896U (en) | 2018-11-23 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201820586157.0U Active CN208135896U (en) | 2018-04-24 | 2018-04-24 | Skid-mounted type methanol and vapor plasma method reformation hydrogen production device of air |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111056532A (en) * | 2020-02-26 | 2020-04-24 | 上海舵杰汽车检测仪器有限公司 | Methanol decomposition hydrogen production device |
| CN113772623A (en) * | 2021-09-16 | 2021-12-10 | 珠海天汇能源科技有限公司 | Methanol skid-mounted hydrogen production machine and hydrogen production method thereof |
-
2018
- 2018-04-24 CN CN201820586157.0U patent/CN208135896U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111056532A (en) * | 2020-02-26 | 2020-04-24 | 上海舵杰汽车检测仪器有限公司 | Methanol decomposition hydrogen production device |
| CN113772623A (en) * | 2021-09-16 | 2021-12-10 | 珠海天汇能源科技有限公司 | Methanol skid-mounted hydrogen production machine and hydrogen production method thereof |
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