CN204625796U - The producer of fuel hydrogen - Google Patents

The producer of fuel hydrogen Download PDF

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Publication number
CN204625796U
CN204625796U CN201520244181.2U CN201520244181U CN204625796U CN 204625796 U CN204625796 U CN 204625796U CN 201520244181 U CN201520244181 U CN 201520244181U CN 204625796 U CN204625796 U CN 204625796U
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CN
China
Prior art keywords
producer
fuel hydrogen
temperature control
communicated
control meter
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201520244181.2U
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Chinese (zh)
Inventor
戴永军
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shenyang Henghui Energy Equipment Co Ltd
Original Assignee
Shenyang Henghui Energy Equipment Co Ltd
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Filing date
Publication date
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Priority to CN201520244181.2U priority Critical patent/CN204625796U/en
Application granted granted Critical
Publication of CN204625796U publication Critical patent/CN204625796U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

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  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

The utility model specifically provides a kind of producer of fuel hydrogen, comprises framework, producer, temperature control meter, airway, supply lead, electric control box.The utility model adopts low-voltage variable frequency, Controlling System and multi-cavity right cylinder separator.Multi-cavity right cylinder separator is not adopting under operations involving high pressure environment, and continuous electrolysis realizes hydrogen or oxygen gas and separates.Owing to adopting low pressure operation, the energy high degree of consumption reduces; In synchronizer, each cylinder produces concussion impulse magnetization by different low voltages, and the positive and negative charge ordered arrangement in the water molecules after being magnetized, reduces the energy of intermolecular covalent linkage.The utility model adopts cartridge type feedback signal to control the electrolytic process of water molecules, and in whole set process flow process, drum separator meeting continuous operation, ensure that the utility model is worked continuously.

Description

The producer of fuel hydrogen
Technical field
The utility model relates to energy utilization equipment, specifically provides a kind of producer of fuel hydrogen.
Background technology
Along with global industry process deepens continuously, the Nonrenewable energy resources such as petrochemical industry show state in short supply.And in the middle of fossil energy use procedure, the perfect problem of many needs such as quantity of heat production is low, utilization rate of heat value is low appears in face of us.But in the drawbacks such as Energy harvesting is low, because burning fossil energy causes the phenomenon of environmental pollution to be on the rise, our nerve challenged one after another in the responsive vocabulary such as acid rain, haze, greenhouse gases, oxynitrides.At present, the clean energies such as hydrogen energy source are used to become one of the pollution that controls environment, the important means improving heat utilization ratio, although achieved significant achievement in hydrogen is produced, but gas production rate is little, it is inconvenient to control, the heat-resisting problem such as not strong of equipment still needs to solve.
Summary of the invention
The utility model provides energy utilization equipment, specifically provides a kind of producer of fuel hydrogen.
The utility model specifically provides a kind of producer of fuel hydrogen, comprises framework 1, producer 3, temperature control meter 4, airway 7, supply lead 8, electric control box 9; Framework 1 entirety is cabinet type structure, and aforementioned structure is arranged in framework 1 except framework 1; Producer 3 is by the extraneous water-supply line of pipeline connection, and airway 7 one end is communicated with producer 3, and the other end is communicated with collection device or supply combustion plant combustion chamber; Temperature control meter 4 one end is arranged in producer 3, and the other end is arranged in outside producer 3; Supply lead 8 connects producer 3 and electric control box 9; Self controlling valve 2 is by cross current producer 3.
Described producer 3 is many body structures, and each producer casing is stand-alone configuration, with other producer casings without direct connected relation.Described producer 3 uses in groups.Described producer 3 be specially polystyle structure and or multiple-piece structure.
The producer of described fuel hydrogen is also provided with escape pipe 10, and escape pipe 10 is arranged in framework 1 upper strata, and airway 7 is communicated with escape pipe 10 bottom through collecting, and escape pipe 10 top is communicated with collection device or supply combustion plant combustion chamber.
The producer of described fuel hydrogen is also provided with spark arrester 11, and spark arrester 11 is arranged between airway 7 and escape pipe 10.
The producer of described fuel hydrogen is also provided with catch basin 12, and catch basin 12 is arranged on the upper strata of framework 1, and the pipeline being communicated with producer 3 connects extraneous water-supply line by catch basin 12.
The producer of described fuel hydrogen is also provided with Self controlling valve 2, cooling tank 5 and cooling line 6; Cooling tube 6 is communicated with cooling tank 5 and producer 3, and Self controlling valve 2 is arranged on cooling tube 6; Self controlling valve 2 is electrically connected temperature control meter 4 and is arranged in one end outside producer 3, and cooling line 6 is communicated with producer 3 by Self controlling valve 2 simultaneously; In described cooling tank 5, water pump is set.
Described electric control box 9 is electrically connected the positive and negative electrode of electrolytic strip or electrolysis post in producer 3.
Formula temperature control meter that described temperature control meter 4 is thermopair temperature control meter, Kick type temperature control meter, liquid rise, compression-type temperature controller, electromagnetic type temperature controller one of them or its combination, each producer 3 casing all arranges a temperature control meter 4.
The utility model adopts low-voltage variable frequency, Controlling System and multi-cavity right cylinder separator or multiple-piece separator.Multi-cavity right cylinder separator or multiple-piece separator are not adopting under operations involving high pressure environment, and continuous electrolysis realizes hydrogen or oxygen gas and separates.Owing to adopting low pressure operation, the energy high degree of consumption reduces; In synchronizer 3, each cylinder produces concussion impulse magnetization by different low voltages, and the positive and negative charge ordered arrangement in the water molecules after being magnetized, reduces the energy of intermolecular covalent linkage.The utility model adopts cartridge type feedback signal to control the electrolytic process of water molecules, and in whole set process flow process, drum separator meeting continuous operation, ensure that the utility model is worked continuously.
In addition, when in producer, temperature is too high, temperature control meter is by warming signal transmission to Self controlling valve, and Self controlling valve is opened, and the electrolytic solution in producer is delivered to cooling tank and carries out naturally cooling.Until the electrolyte temperature in producer is down to 45 DEG C to 75 DEG C periods, Self controlling valve quits work.
Each producer casing is all communicated with cooling tank by cooling line.
The utility model can be widely used in the technical fields such as hydrogen fuel cell manufacture, oil, metallurgy, chemical industry, food, medicine, coal, the energy, aerospace, can also relate to the manufacture fields such as glass-ceramic, unicircuit, automobile, boats and ships simultaneously.Briefly, the utility model can penetrate into each and relate to energy consumption or each large technical field provided and industry, is with a wide range of applications and the value of environmental protection.
Experimentally obtain as drawn a conclusion: using the gas fired-boiler of 10t level or more, even big power station's boiler, coal firing boiler, oil-firing boiler, biological combustion matter boiler, stalk fire boiler or vehicle, the engines for boat such as matter boiler, be mixed into the gas that volume fraction is 25% the utility model generation, burning cost 24% or more can be reduced, reduce harmful gas emission 95% or more, high degree has saved the energy, reduce production cost, serve extremely strong environmental benefit simultaneously.
Accompanying drawing explanation
Below in conjunction with accompanying drawing, the utility model is described in further detail.
Fig. 1 is the producer one-piece construction schematic diagram of fuel hydrogen;
Fig. 2 is the producer one-piece construction rear view schematic diagram of fuel hydrogen.
Embodiment
Reference numeral illustrates:
Framework 1, Self controlling valve 2, producer 3, temperature control meter 4, cooling tank 5, cooling line 6, airway 7, supply lead 8, electric control box 9, escape pipe 10, spark arrester 11, catch basin 12.
Embodiment 1
Present embodiments provide energy utilization equipment, specifically provide a kind of producer of fuel hydrogen.
The present embodiment specifically provides a kind of producer of fuel hydrogen, comprises framework 1, producer 3, temperature control meter 4, airway 7, supply lead 8, electric control box 9; Framework 1 entirety is cabinet type structure, and aforementioned structure is arranged in framework 1 except framework 1; Producer 3 is by the extraneous water-supply line of pipeline connection, and airway 7 one end is communicated with producer 3, and the other end is communicated with collection device or supply combustion plant combustion chamber; Temperature control meter 4 one end is arranged in producer 3, and the other end is arranged in outside producer 3; Supply lead 8 connects producer 3 and electric control box 9; Self controlling valve 2 is by cross current producer 3.
Described producer 3 is many body structures, and each producer casing is stand-alone configuration, with other producer casings without direct connected relation.Described producer 3 uses in groups.Described producer 3 be specially polystyle structure and or multiple-piece structure.
The producer of described fuel hydrogen is also provided with escape pipe 10, and escape pipe 10 is arranged in framework 1 upper strata, and airway 7 is communicated with escape pipe 10 bottom through collecting, and escape pipe 10 top is communicated with collection device or supply combustion plant combustion chamber.
The producer of described fuel hydrogen is also provided with spark arrester 11, and spark arrester 11 is arranged between airway 7 and escape pipe 10.
The producer of described fuel hydrogen is also provided with catch basin 12, and catch basin 12 is arranged on the upper strata of framework 1, and the pipeline being communicated with producer 3 connects extraneous water-supply line by catch basin 12.
The producer of described fuel hydrogen is also provided with Self controlling valve 2, cooling tank 5 and cooling line 6; Cooling tube 6 is communicated with cooling tank 5 and producer 3, and Self controlling valve 2 is arranged on cooling tube 6; Self controlling valve 2 is electrically connected temperature control meter 4 and is arranged in one end outside producer 3, and cooling line 6 is communicated with producer 3 by Self controlling valve 2 simultaneously; In described cooling tank 5, water pump is set.
Described electric control box 9 is electrically connected the positive and negative electrode of electrolytic strip or electrolysis post in producer 3.
Formula temperature control meter that described temperature control meter 4 is thermopair temperature control meter, Kick type temperature control meter, liquid rise, compression-type temperature controller, electromagnetic type temperature controller one of them or its combination, each producer 3 casing all arranges a temperature control meter 4.
The present embodiment adopts low-voltage variable frequency, Controlling System and multi-cavity right cylinder separator or multiple-piece separator.Multi-cavity right cylinder separator or multiple-piece separator are not adopting under operations involving high pressure environment, and continuous electrolysis realizes hydrogen or oxygen gas and separates.Owing to adopting low pressure operation, the energy high degree of consumption reduces; In synchronizer 3, each cylinder produces concussion impulse magnetization by different low voltages, and the positive and negative charge ordered arrangement in the water molecules after being magnetized, reduces the energy of intermolecular covalent linkage.The present embodiment adopts cartridge type feedback signal to control the electrolytic process of water molecules, and in whole set process flow process, drum separator meeting continuous operation, ensure that the present embodiment is worked continuously.
In addition, when in producer, temperature is too high, temperature control meter is by warming signal transmission to Self controlling valve, and Self controlling valve is opened, and the electrolytic solution in producer is delivered to cooling tank and carries out naturally cooling.Until the electrolyte temperature in producer is down to 45 DEG C to 75 DEG C periods, Self controlling valve quits work.
Each producer casing is all communicated with cooling tank by cooling line.
The present embodiment can be widely used in the technical fields such as hydrogen fuel cell manufacture, oil, metallurgy, chemical industry, food, medicine, coal, the energy, aerospace, can also relate to the manufacture fields such as glass-ceramic, unicircuit, automobile, boats and ships simultaneously.Briefly, the present embodiment can penetrate into each and relate to energy consumption or each large technical field provided and industry, is with a wide range of applications and the value of environmental protection.
Experimentally obtain as drawn a conclusion: using the gas fired-boiler of 10t level or more, even big power station's boiler, coal firing boiler, oil-firing boiler, biological combustion matter boiler, stalk fire boiler or vehicle, the engines for boat such as matter boiler, be mixed into the gas that volume fraction is 25% the present embodiment generation, burning cost 24% or more can be reduced, reduce harmful gas emission 95% or more, high degree has saved the energy, reduce production cost, serve extremely strong environmental benefit simultaneously.
Embodiment 2
The present embodiment specifically uses electromagnetic type temperature control meter as temperature control meter, and all the other structures, technical scheme, desired result are identical with embodiment 1.
Embodiment 3
The present embodiment is not except arranging catch basin 12, and all the other structures, technical scheme, desired result are identical with embodiment 2.
Embodiment 4
The present embodiment is not except arranging cooling tank 5, water-cooled tube 6, and all the other structures, technical scheme, desired result are identical with embodiment 2.
Embodiment 5
The present embodiment is not except producer 3 uses in groups, and all the other structures, technical scheme, desired result are identical with embodiment 2.
Embodiment 6
The present embodiment except producer 3 be integral type producer but not split stand alone type producer except, all the other structures, technical scheme, desired result are identical with embodiment 2.
Embodiment 7
The present embodiment is not except arranging spark arrester 11, and all the other structures, technical scheme, desired result are identical with embodiment 2.
Above-described embodiment, only for technical conceive and the feature of the present embodiment are described, its object is to person skilled in the art can be understood the content of the present embodiment and implement according to this, can not limit the protection domain of the present embodiment with this.All equivalence changes of doing according to the present embodiment spirit or modify, within the protection domain that all should be encompassed in the present embodiment.

Claims (10)

1. a producer for fuel hydrogen, is characterized in that comprising framework (1), producer (3), temperature control meter (4), airway (7), supply lead (8), electric control box (9); Framework (1) entirety is cabinet type structure, and aforementioned structure is arranged in framework (1) except framework (1); Producer (3) is by the extraneous water-supply line of pipeline connection, and airway (7) one end is communicated with producer (3), and the other end is communicated with collection device or supply combustion plant combustion chamber; Temperature control meter (4) one end is arranged in producer (3), and the other end is arranged in producer (3) outward; Supply lead (8) connects producer (3) and electric control box (9); Self controlling valve (2) is by cross current producer (3).
2. the producer of fuel hydrogen according to claim 1, it is characterized in that described producer (3) is many body structures, each producer casing is stand-alone configuration, with other producer casings without direct connected relation.
3. the producer of fuel hydrogen according to claim 1 and 2, is characterized in that described producer (3) uses in groups.
4. the producer of fuel hydrogen according to claim 1 and 2, it is characterized in that described producer (3) be specially polystyle structure and or multiple-piece structure.
5. the producer of fuel hydrogen according to claim 1, it is characterized in that the producer of described fuel hydrogen is also provided with escape pipe (10), escape pipe (10) is arranged in framework (1) upper strata, airway (7) is communicated with escape pipe (10) bottom through collecting, and escape pipe (10) top is communicated with collection device or supply combustion plant combustion chamber.
6. the producer of fuel hydrogen according to claim 1 or 5, it is characterized in that the producer of described fuel hydrogen is also provided with spark arrester (11), spark arrester (11) is arranged between airway (7) and escape pipe (10).
7. the producer of the fuel hydrogen according to claim 1 or 2 or 5, it is characterized in that the producer of described fuel hydrogen is also provided with catch basin (12), catch basin (12) is arranged on the upper strata of framework (1), and the pipeline being communicated with producer (3) connects extraneous water-supply line by catch basin (12).
8. the producer of the fuel hydrogen according to claim 1 or 2 or 5, is characterized in that the producer of described fuel hydrogen is also provided with Self controlling valve (2), cooling tank (5) and cooling line (6); Cooling line (6) is communicated with cooling tank (5) and producer (3), and Self controlling valve (2) is arranged on cooling line (6); Self controlling valve (2) electrical connection temperature control meter (4) is arranged in producer (3) one end outward, and cooling line (6) is communicated with producer (3) by Self controlling valve (2) simultaneously; In described cooling tank (5), water pump is set.
9. the producer of the fuel hydrogen according to claim 1 or 2 or 5, is characterized in that the positive and negative electrode of electrolytic strip or electrolysis post in described electric control box (9) electrical connection producer (3).
10. the producer of fuel hydrogen according to claim 8, it is characterized in that described temperature control meter (4) is thermopair temperature control meter, Kick type temperature control meter, liquid rise by formula temperature control meter, compression-type temperature controller, electromagnetic type temperature controller one of them or its combination, each producer (3) casing all arranges a temperature control meter (4).
CN201520244181.2U 2015-04-21 2015-04-21 The producer of fuel hydrogen Expired - Fee Related CN204625796U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520244181.2U CN204625796U (en) 2015-04-21 2015-04-21 The producer of fuel hydrogen

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201520244181.2U CN204625796U (en) 2015-04-21 2015-04-21 The producer of fuel hydrogen

Publications (1)

Publication Number Publication Date
CN204625796U true CN204625796U (en) 2015-09-09

Family

ID=54044842

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201520244181.2U Expired - Fee Related CN204625796U (en) 2015-04-21 2015-04-21 The producer of fuel hydrogen

Country Status (1)

Country Link
CN (1) CN204625796U (en)

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20150909

Termination date: 20160421