CN108190833A - A kind of production system of water base hydrogen energy source in situ - Google Patents
A kind of production system of water base hydrogen energy source in situ Download PDFInfo
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- CN108190833A CN108190833A CN201810160729.3A CN201810160729A CN108190833A CN 108190833 A CN108190833 A CN 108190833A CN 201810160729 A CN201810160729 A CN 201810160729A CN 108190833 A CN108190833 A CN 108190833A
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- Prior art keywords
- metering device
- fuel
- storage tank
- delivery pipe
- conversion chamber
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- 239000001257 hydrogen Substances 0.000 title claims abstract description 55
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 55
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 54
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 45
- 238000011065 in-situ storage Methods 0.000 title claims abstract description 28
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 22
- 239000000446 fuel Substances 0.000 claims abstract description 53
- 238000006243 chemical reaction Methods 0.000 claims abstract description 45
- 238000003860 storage Methods 0.000 claims abstract description 37
- 239000007789 gas Substances 0.000 claims abstract description 36
- 239000003995 emulsifying agent Substances 0.000 claims abstract description 31
- 239000007788 liquid Substances 0.000 claims abstract description 19
- 239000000839 emulsion Substances 0.000 claims abstract description 12
- 239000008399 tap water Substances 0.000 claims abstract description 8
- 235000020679 tap water Nutrition 0.000 claims abstract description 8
- 238000004945 emulsification Methods 0.000 claims abstract description 4
- 239000002994 raw material Substances 0.000 claims abstract description 4
- 238000009834 vaporization Methods 0.000 claims abstract description 4
- 230000008016 vaporization Effects 0.000 claims abstract description 4
- 239000002737 fuel gas Substances 0.000 claims description 9
- 230000008859 change Effects 0.000 claims description 8
- 239000006185 dispersion Substances 0.000 claims description 3
- 230000001804 emulsifying effect Effects 0.000 claims description 3
- 238000010008 shearing Methods 0.000 claims description 3
- 239000006210 lotion Substances 0.000 claims 1
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 230000032258 transport Effects 0.000 description 6
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 230000008676 import Effects 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000004577 artificial photosynthesis Methods 0.000 description 1
- 210000000481 breast Anatomy 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 235000010299 hexamethylene tetramine Nutrition 0.000 description 1
- VKYKSIONXSXAKP-UHFFFAOYSA-N hexamethylenetetramine Chemical compound C1N(C2)CN3CN1CN2C3 VKYKSIONXSXAKP-UHFFFAOYSA-N 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 229960004011 methenamine Drugs 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000012286 potassium permanganate Substances 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 238000005809 transesterification reaction Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/04—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of inorganic compounds, e.g. ammonia
- C01B3/042—Decomposition of water
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
- C10L3/12—Liquefied petroleum gas
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/0266—Processes for making hydrogen or synthesis gas containing a decomposition step
- C01B2203/0277—Processes for making hydrogen or synthesis gas containing a decomposition step containing a catalytic decomposition step
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/06—Integration with other chemical processes
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/08—Methods of heating or cooling
- C01B2203/0805—Methods of heating the process for making hydrogen or synthesis gas
- C01B2203/0811—Methods of heating the process for making hydrogen or synthesis gas by combustion of fuel
- C01B2203/0816—Heating by flames
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/10—Catalysts for performing the hydrogen forming reactions
- C01B2203/1041—Composition of the catalyst
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/12—Feeding the process for making hydrogen or synthesis gas
- C01B2203/1205—Composition of the feed
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/02—Combustion or pyrolysis
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Hydrogen, Water And Hydrids (AREA)
Abstract
The present invention relates to a kind of production system of water base hydrogen energy source in situ, including magma storage tank, originally the first metering device, water pot, the second metering device, fuel emulsifier device, third metering device, conversion chamber, liquid gas storage tank, the 4th metering device and special nozzle.Raw material in magma storage tank is delivered to after the metering of the first metering device in fuel emulsifier device；Originally the tap water in water pot is delivered to after the metering of the second metering device in fuel emulsifier device；Magma and the tap water of originally water pot conveying of the emulsifier unit for being conveyed to magma storage tank carry out emulsification treatment, and form fuel emulsion, vaporization in conversion chamber is delivered to after the metering of third metering device and forms gas, liquefied gas in liquid gas storage tank is delivered to special nozzle by the 4th metering device, and special nozzle mixes liquefied gas and gas and realizes ignition.The beneficial effects of the present invention are provide a kind of production system of low cost, safe and reliable and energy-saving and environment-friendly water base hydrogen energy source in situ.
Description
Technical field
The present invention relates to a kind of production systems of water base hydrogen energy source in situ.
Background technology
Scientist finds that hydrogen is optimal fuel on the earth very early.The utilization of hydrogen fuel, when it is inexpensive, second is that will
Safety, this is two keys.That is, for using hydrogen fuel, one is able to solve the problems, such as inexpensively to obtain hydrogen fuel, and two are able to
It solves the problems, such as the safe storage of hydrogen fuel, transport safely and use safely.
Instantly, hydrogen energy source upsurge is risen in the world, there is from oil hydrogen manufacturing, artificial photosynthesis' aqueous solution in hydrogen manufacturing, coal
Middle hydrogen manufacturing ... type is relatively more.But common problem is：There is peaces for production, storage, transport, the burning of hydrogen
Full hidden danger.The engineering of hydrogen manufacturing is complicated, and investment is huge, the drawbacks of being more than actual effect there are concept.It solves the problems, such as these, allows ideal
Hydrogen becomes the commonly used energy, far away.
Invention content
In view of the above-mentioned problems in the prior art, it is a primary object of the present invention to provide a kind of of low cost, section
The production system of water base hydrogen energy source in situ that can be environmentally friendly and safe and reliable.
The present invention provides a kind of production system of water base hydrogen energy source in situ, including magma storage tank, the first metering device, from
Come water pot, the second metering device, fuel emulsifier device, third metering device, conversion chamber, liquid gas storage tank, the 4th metering device with
And special nozzle, wherein：
The magma storage tank is used to store magma；
First metering device is connected respectively with the magma storage tank and the fuel emulsifier device, the magma storage
Raw material in tank is delivered to after first metering device metering in fuel emulsifier device；
Second metering device is connected respectively with the originally water pot and the fuel emulsifier device, the tap water
Tap water in tank is delivered to after second metering device metering in the fuel emulsifier device；
The fuel emulsifier device conveys originally for the magma conveyed to the magma storage tank and the originally water pot
Water carries out emulsification treatment, and forms fuel emulsion；
The third metering device is connected respectively with the fuel emulsifier device and Suo Shu Zhuan Change chambers, the fuel emulsifier
Fuel emulsion in device is delivered to after the metering of third metering device in the conversion chamber, the fuel emulsion Suo Shu Zhuan Change
Vaporization forms gas in chamber, and the special nozzle is also connected with the conversion chamber；
4th metering device is connected respectively with the liquid gas storage tank and special nozzle, the liquid in the liquid gas storage tank
Change gas and special nozzle is delivered to by the 4th metering device, the special nozzle is used for the liquefied gas conveyed to liquid gas storage tank
It is mixed with the gas of the conversion chamber conveying and realizes ignition.
The fuel emulsifier device is high-shearing dispersion emulsifying machine.
The conversion chamber is located at the external side of the special nozzle, and the conversion chamber includes conversion chamber ontology, described
The both ends of conversion chamber ontology are closed, and the first delivery pipe and the second delivery pipe are provided in the conversion chamber ontology, wherein, it is described
The left end of first delivery pipe is connected by fuel emulsion delivery pipe with the third metering device, and first delivery pipe
Right end is arranged on the conversion chamber body interior, and the left end of second delivery pipe is connected with the fuel gas inlet of the special nozzle
It is logical, and the right end of second delivery pipe is arranged on the inside of the conversion chamber ontology.
Left end flush of the left end of first delivery pipe and the second delivery pipe with the conversion chamber ontology, and it is described
The length of first delivery pipe is more than the length of second delivery pipe.
The left end of second delivery pipe is connected by the first appendix with the fuel gas inlet of the special nozzle.
4th metering device is connected by the second appendix with the fuel gas inlet of the special nozzle.
The present invention has the following advantages and beneficial effect：Patent of the present invention solves the problems, such as the cheap acquisition of hydrogen fuel, together
When also solve the problems, such as the safe storage of hydrogen fuel, transport safely and use safely, this just make hydrogen energy source in situ become can be general
All over the new energy of application；It has the characteristics that save energy consumption cost, reduce disposal of pollutants and save oil gas resource.
Description of the drawings
Fig. 1 is the structure diagram of the production system of water base hydrogen energy source in situ provided in an embodiment of the present invention；
Fig. 2 is the main structure diagram that chamber is converted in Fig. 1；
Fig. 3 is the left view structural representation that chamber is converted in Fig. 1；
Fig. 4 is conversion chamber and the matched structure diagram of special nozzle in Fig. 1.
Specific embodiment
Purpose, technical scheme and advantage to make the embodiment of the present invention are clearer, below in conjunction with the embodiment of the present invention
In attached drawing, the technical solution in the embodiment of the present invention is clearly and completely described, it is clear that described embodiment is
Part of the embodiment of the present invention, instead of all the embodiments.The present invention being usually described and illustrated herein in the accompanying drawings is implemented
The component of example can be configured to arrange and design with a variety of different.Therefore, below to provide in the accompanying drawings the present invention reality
The detailed description for applying example is not intended to limit the range of claimed invention, but is merely representative of the selected implementation of the present invention
Example.Based on the embodiments of the present invention, those of ordinary skill in the art are obtained without creative efforts
Every other embodiment, shall fall within the protection scope of the present invention.
The present invention is further illustrated with specific embodiment below with reference to accompanying drawings.
As shown in Figures 1 to 4：A kind of production system of water base hydrogen energy source in situ of the embodiment of the present invention, is stored up including magma
Tank 101, originally the first metering device 102, water pot 103, the second metering device 104, fuel emulsifier device 105, third metering dress
106, conversion chamber 107, liquid gas storage tank 109, the 4th metering device 110 and special nozzle 108 are put, wherein：
The magma storage tank 101 is for storing magma, and the magma is solvent and the mixture of catalyst, wherein solvent
For alcohol, ketone, alkane, alkenes solvent, the catalyst is potassium permanganate, second-benzyl carbinol, sodium chloride, one kind in methenamine or
It is a variety of；
First metering device 102 is connected respectively with the magma storage tank 101 and the fuel emulsifier device 105,
Raw material in the magma storage tank 101 is delivered to after first metering device 102 metering in fuel emulsifier device 105；
Second metering device 104 is connected respectively with the originally water pot 103 and the fuel emulsifier device 105,
Tap water in the originally water pot 103 is delivered to the fuel emulsifier device 105 after second metering device 104 metering
In；
Magma and the originally water pot 103 of the fuel emulsifier device 105 for being conveyed to the magma storage tank 101 are defeated
The tap water sent carries out emulsification treatment, and forms fuel emulsion；
The third metering device 106 is connected respectively with the fuel emulsifier device 105 and Suo Shu Zhuan Change chambers 107, institute
It states the fuel emulsion in fuel emulsifier device 105 to be delivered to after the metering of third metering device 106 in the conversion chamber 107, institute
It states vaporization in fuel emulsion Suo Shu Zhuan Change chambers 107 and forms gas, the special nozzle 108 is also connected with the conversion chamber 107
It is logical；
4th metering device 110 is connected respectively with the liquid gas storage tank 109 and special nozzle 108, the liquefaction
Liquefied gas in gas tank 109 is delivered to special nozzle 108 by the 4th metering device 110, and the special nozzle 108 is used for
The gas that the liquefied gas and the conversion chamber 107 conveyed to liquid gas storage tank 109 conveys is mixed and realizes ignition.
The fuel emulsifier device 105 is high-shearing dispersion emulsifying machine.
The conversion chamber 107 is located at the external side of the special nozzle 108, and the conversion chamber 107 includes conversion chamber
Ontology 1071, as shown in Figures 2 and 3, the both ends of the conversion chamber ontology 1071 are closed, and are set in the conversion chamber ontology 1071
The first delivery pipe 1072 and the second delivery pipe 1073 are equipped with, wherein, the left end of first delivery pipe 1072 passes through fuel emulsion
Delivery pipe 111 is connected with the third metering device 106, and the right end of first delivery pipe 1072 is arranged on the conversion
Inside chamber ontology 1071, the left end of second delivery pipe 1073 is connected with the fuel gas inlet of the special nozzle 108, and institute
The right end for stating the second delivery pipe 1073 is arranged on the inside of the conversion chamber ontology 1071；Meanwhile the conversion chamber 107 and special
Burner 108 can be arranged in burner hearth 114, as shown in Figure 4.
Left end of the left end of first delivery pipe, 1072 and second delivery pipe 1073 with the conversion chamber ontology 1071
Flush, and the length of first delivery pipe 1072 is more than the length of second delivery pipe 1073.
The fuel gas inlet that the left end of second delivery pipe 1073 passes through the first appendix 112 and the special nozzle 108
It is connected.
4th metering device 110 is connected by the second appendix 113 with the fuel gas inlet of the special nozzle 108
It is logical.
The production system of water base hydrogen energy source in situ provided in an embodiment of the present invention, (water purification, waste water or sea can be used using water
Water) as base stock, under magma effect, water is made to carry out the water situ combustion of conversion and hydrogen in situ.That is, needing Hydrogen Energy
Water (i.e. on the spot) is converted to hydrogen energy source by the original position (i.e. on the spot) in source immediately in situ, and just in the original position for needing hydrogen energy source (i.e.
Carry out hydrogen energy source burning immediately on the spot).Original position in the conversion of water original position and the original position in the situ combustion of hydrogen are same in situ, same
One on the spot, transport and storage problem there is no hydrogen energy source, also just transports and stores dangerous or dangerous there is no hydrogen energy source
Problem.It is discussed in situ here it is hydrogen fuel.
Patent of the present invention solves the production cost of hydrogen energy source, is actually solved by " conversion in situ of water ", utilizes water
(water purification, waste water or seawater can be used) as base stock, under magma effect, make water carry out water in-situ transesterification change become it is cheap and
The hydrogen energy source being easy to get.
It as the transporting safely of hydrogen energy source, stores and using this problem, the art of this patent is actually by " the original position of water
Conversion and the situ combustion of hydrogen " naturally solves, because being in the original position (i.e. on the spot) for needing hydrogen energy source that water is in situ
Hydrogen energy source is converted to, and carries out the burning of hydrogen energy source immediately in the original position for needing hydrogen energy source again, that is, " instant generating and using ", no
Transport and storage problem there are hydrogen energy source.Ensured using the safety of problem by conversion chamber, it is necessary at 500 degrees Celsius
Become the gas of flammable state by the liquid of non-combustible liquid.The liquid of non-combustible liquid is very safe, the breast of this High water cut point
Liquid does not have toxicity, without corrosivity, even if having open fire that will not light at less than 300 degree Celsius, will not exploding, is highly convenient for pacifying
Full storage and transportation and use.
Patent of the present invention solves the problems, such as the cheap acquisition of hydrogen fuel, while also solves the safe storage of hydrogen fuel, peace
It is for the national games it is defeated and safe handling problem, this just make hydrogen energy source in situ become can be commonly used new energy.
Patent of the present invention solves the problems, such as following three aspects：
1st, energy consumption cost is saved
Hydrogen energy source in situ can replace 50% oil gas completely, save energy consumption cost 40% or so.
2nd, disposal of pollutants is reduced
Predominant emissions after being burnt due to hydrogen energy source in situ are water vapours, so it can purify air, reduce a large amount of nitrogen
Oxide enters air.
3rd, oil gas resource is saved
From 3,500,000 tons of import volume in 2008, surged by 2014 to 198,470,000 tons.One month 2016 with regard to import 523
Ten thousand tons.This accounts for 30% or so of national dosage, other to be solved by domestic self-produced air source.If hydrogen energy source in situ can be widely used,
More than 50% oil gas is substituted, it is extremely considerable to save oil gas resource quantity.
Finally it should be noted that：Above-described embodiments are merely to illustrate the technical scheme rather than to it
Limitation；Although the present invention is described in detail referring to the foregoing embodiments, it will be understood by those of ordinary skill in the art that：
It can still modify to the technical solution recorded in previous embodiment or to which part or all technical features into
Row equivalent replacement；And these modifications or substitutions, it does not separate the essence of the corresponding technical solution various embodiments of the present invention technical side
The range of case.
Claims (6)
1. a kind of production system of water base hydrogen energy source in situ, which is characterized in that including magma storage tank, the first metering device, originally
Water pot, the second metering device, fuel emulsifier device, third metering device, conversion chamber, liquid gas storage tank, the 4th metering device and
Special nozzle, wherein：
The magma storage tank is used to store magma；
First metering device is connected respectively with the magma storage tank and the fuel emulsifier device, in the magma storage tank
Raw material through first metering device metering after be delivered in fuel emulsifier device；
Second metering device is connected respectively with the originally water pot and the fuel emulsifier device, in the originally water pot
Tap water through second metering device metering after be delivered in the fuel emulsifier device；
The tap water that the fuel emulsifier device is used for magma convey to the magma storage tank and the originally water pot conveys into
Row emulsification treatment, and form fuel emulsion；
The third metering device is connected respectively with the fuel emulsifier device and Suo Shu Zhuan Change chambers, the fuel emulsifier device
In fuel emulsion through third metering device metering after be delivered to it is described conversion chamber in, in the fuel emulsion Suo Shu Zhuan Change chambers
Vaporization forms gas, and the special nozzle is also connected with the conversion chamber；
4th metering device is connected respectively with the liquid gas storage tank and special nozzle, the liquefied gas in the liquid gas storage tank
Special nozzle is delivered to by the 4th metering device, the special nozzle is used for the liquefied gas conveyed to liquid gas storage tank and institute
The gas for stating conversion chamber conveying is mixed and realizes ignition.
2. the production system of water base hydrogen energy source in situ according to claim 1, which is characterized in that the fuel emulsifier device
For high-shearing dispersion emulsifying machine.
3. the production system of water base hydrogen energy source in situ according to claim 1, which is characterized in that the conversion chamber is located at institute
The external side of special nozzle is stated, and the conversion chamber includes conversion chamber ontology, the both ends of the conversion chamber ontology are closed, institute
It states in conversion chamber ontology and is provided with the first delivery pipe and the second delivery pipe, wherein, the left end of first delivery pipe passes through fuel
Lotion delivery pipe is connected with the third metering device, and the right end of first delivery pipe is arranged on the conversion chamber ontology
Inside, the left end of second delivery pipe are connected with the fuel gas inlet of the special nozzle, and the right side of second delivery pipe
End is arranged on the inside of the conversion chamber ontology.
4. the production system of water base hydrogen energy source in situ according to claim 3, which is characterized in that first delivery pipe and
Left end flush of the left end of second delivery pipe with the conversion chamber ontology, and the length of first delivery pipe is more than described
The length of second delivery pipe.
5. the production system of water base hydrogen energy source in situ according to claim 4, which is characterized in that second delivery pipe
Left end is connected by the first appendix with the fuel gas inlet of the special nozzle.
6. the production system of water base hydrogen energy source in situ according to claim 5, which is characterized in that the 4th metering device
It is connected by the second appendix with the fuel gas inlet of the special nozzle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810160729.3A CN108190833A (en) | 2018-02-27 | 2018-02-27 | A kind of production system of water base hydrogen energy source in situ |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810160729.3A CN108190833A (en) | 2018-02-27 | 2018-02-27 | A kind of production system of water base hydrogen energy source in situ |
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| Publication Number | Publication Date |
|---|---|
| CN108190833A true CN108190833A (en) | 2018-06-22 |
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| CN201810160729.3A Pending CN108190833A (en) | 2018-02-27 | 2018-02-27 | A kind of production system of water base hydrogen energy source in situ |
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Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
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| CN102533349A (en) * | 2010-12-16 | 2012-07-04 | 刘心灵 | Water-based fuel and combustion method |
| CN102939448A (en) * | 2010-04-16 | 2013-02-20 | E·W·科蒂尔 | Real-time online aqueous fuel emulsification device, method and system |
| CN208545115U (en) * | 2018-02-27 | 2019-02-26 | 任永飞 | A kind of production system of water base hydrogen energy source in situ |
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2018
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| CN1067671A (en) * | 1991-06-12 | 1993-01-06 | 郑锡同 | Hydrolytic hydrogen liquid fucel and manufacturing thereof |
| CN1100189A (en) * | 1994-03-14 | 1995-03-15 | 刘绍之 | Water-based composite fuel and cooker therefor |
| CN2267390Y (en) * | 1995-12-26 | 1997-11-12 | 郑锡同 | Arrangement for evaporating liquid fuel with chemical conversion |
| CN2514229Y (en) * | 2001-11-26 | 2002-10-02 | 王福清 | Emulsified fuel burner for furnace |
| CN1465884A (en) * | 2002-07-03 | 2004-01-07 | 李巧龙 | Fuel random hydrogenated modifying method and device for making gas by water |
| CN102939448A (en) * | 2010-04-16 | 2013-02-20 | E·W·科蒂尔 | Real-time online aqueous fuel emulsification device, method and system |
| CN102533349A (en) * | 2010-12-16 | 2012-07-04 | 刘心灵 | Water-based fuel and combustion method |
| CN208545115U (en) * | 2018-02-27 | 2019-02-26 | 任永飞 | A kind of production system of water base hydrogen energy source in situ |
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