CN207385424U - Automatic control structure raw material decomposes device - Google Patents

Automatic control structure raw material decomposes device Download PDF

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Publication number
CN207385424U
CN207385424U CN201721351668.6U CN201721351668U CN207385424U CN 207385424 U CN207385424 U CN 207385424U CN 201721351668 U CN201721351668 U CN 201721351668U CN 207385424 U CN207385424 U CN 207385424U
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CN
China
Prior art keywords
box
valve
nitrogen
conduit
raw material
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
CN201721351668.6U
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Chinese (zh)
Inventor
叶建超
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.)
Jiangxi Xinxi Foundry Material Co Ltd
Original Assignee
Jiangxi Xinxi Foundry Material Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Jiangxi Xinxi Foundry Material Co Ltd filed Critical Jiangxi Xinxi Foundry Material Co Ltd
Priority to CN201721351668.6U priority Critical patent/CN207385424U/en
Application granted granted Critical
Publication of CN207385424U publication Critical patent/CN207385424U/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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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The utility model discloses automatic control structure raw material decomposes devices,Including material taking mouth,Control panel,Control button,Decompose tank,Liquefied ammonia entrance,Nitrogen conduit,Case lid,Collecting box,First valve,Electric drive hydraulic thruster,Lanthanum nickel metal derby,Purify case,Adsorbent,Heater,Separator box,Gas separation membrane,Pneumohydraulic pressure-cylinder,Heater box,Catalyst nozzle,Annular conduit,Storage box,Electric pushrod,Second valve,Return pump,Airflow duct and electrothermal tube,Material taking mouth is offered at the top of the decomposition tank,The one side of the material taking mouth is equipped with control panel,The one side of the control panel is equipped with control button,The one side of the control button offers liquefied ammonia entrance,The one side of the liquefied ammonia entrance is equipped with nitrogen conduit,The device,It can not only be by the nitrogen and Hydrogen Separation after decomposition,It and can be by nitrogen recycling,Purification storage can be carried out to hydrogen simultaneously,Obtain better hydrogen feed.

Description

Automatic control structure raw material decomposes device
Technical field
The utility model is related to resolving device technical fields, are specially automatic control structure raw material decomposes device.
Background technology
Hydrogen is industrial common substance, and the preparation of hydrogen is got often through liquid ammonolysis craft, current decomposition dress It puts and is on the one hand not provided with equipment for purifying, so that containing mixed gas in hydrogen obtained, be unfavorable for hydrogen on the raw material of industry Use, on the other hand, these mixed gas also can be used as other industrial raw materials, such as liquid ammonia is generated when decomposing Nitrogen, as a kind of inert gas, available for making nitrogenous fertilizer and synthetic dyestuffs, further, since hydrogen itself unstable and Explosive characteristic, hydrogen is made often has inconvenience in storage and transport, and therefore, it is necessary to a kind of new to automatically control Construction materials decomposers solves the above problems.
Utility model content
The purpose of this utility model is to provide automatic control structure raw material decomposes device, to solve in above-mentioned background technology The problem of proposition.
In order to solve the above-mentioned technical problem, the utility model provides following technical solution:Automatic control structure raw material decomposes Device, including material taking mouth, control panel, control button, decomposition tank, liquefied ammonia entrance, nitrogen conduit, case lid, collecting box, the first valve Door, electric drive hydraulic thruster, lanthanum nickel metal derby, purification case, adsorbent, heater, separator box, gas separation membrane, pneumohydraulic pressure-cylinder, Heater box, catalyst nozzle, annular conduit, storage box, electric pushrod, the second valve, return pump, airflow duct and electrothermal tube, Material taking mouth is offered at the top of the decomposition tank, the one side of the material taking mouth is equipped with control panel, and the one of the control panel Side is equipped with control button, and the one side of the control button offers liquefied ammonia entrance, and the one side of the liquefied ammonia entrance is equipped with nitrogen Airway, the one side of the nitrogen conduit are equipped with collecting box, and the one side of the collecting box is equipped with case lid, the decomposition tank Inside is equipped with heater box, and the inside of the heater box is equipped with electrothermal tube, and the surface wrap of the electrothermal tube has annular conduit, The inside of the annular conduit is equipped with catalyst nozzle, and the heater box is connected by airflow duct with separator box, described point Inside from case is equipped with pneumohydraulic pressure-cylinder, and the one side of the pneumohydraulic pressure-cylinder is equipped with return pump, the one side of the return pump Gas separation membrane is installed, the separator box is connected by airflow duct with purification case, and the inside of the purification case, which is equipped with, to be added Hot device, the inner wall insertion of the purification case are equipped with adsorbent, and the purification case is connected by airflow duct with storage box, described The inside of storage box is equipped with the second valve, and the one side of second valve is equipped with electric pushrod, and the one of the electric pushrod Side is equipped with lanthanum nickel metal derby, and the one side of the lanthanum nickel metal derby is equipped with the first valve, the one side installation of first valve There is electric drive hydraulic thruster, the control panel is electrically connected electric drive hydraulic thruster, electric pushrod and return pump.
Further, the annular conduit is connected by ring flange with decomposing the one side inner wall of tank.
Further, the electric drive hydraulic thruster is connected by screw with decomposing the one side inner wall of tank.
Further, first valve is connected by slide with storage box.
Compared with prior art, the advantageous effect that the utility model is reached is:The automatic control structure raw material decomposes fill It puts, during using the device, first passes through control button starter, then liquid ammonia is poured by liquefied ammonia entrance in annular conduit, Since annular conduit is wound around the surface of electrothermal tube, liquid ammonia can flow through annular conduit with uniform speed slow, convenient for liquid State ammonia is fully heated, while the catalyst nozzle inside annular conduit can spray catalyst, and liquid ammonia is in the work of high mild catalytic Under, nitrogen, hydrogen and a small amount of steam can be resolved into, since the density of nitrogen and hydrogen is less than air, two kinds of gaseous mixtures Cognition enters along airflow duct in separator box, and the pneumohydraulic pressure-cylinder inside separator box can increase the pressure inside separator box, make The permeability for obtaining gas separation membrane changes, so that hydrogen can be by gas separation membrane, and nitrogen is then left on separation In case, the hydrogen after separation continues on airflow duct and enters purification case, in the hydrogen after decomposition still containing a small amount of nitrogen and Steam, into after purifying case, heater works so that the adsorbent inside purification case fully absorbs nitrogen and water in hydrogen Vapour further obtains more pure hydrogen, after purification, then starts electric pushrod by control button and opens the second valve, So that hydrogen enters in storage box, the lanthanum nickel metal derby inside storage box can be good at absorption of hydrogen and be stored up, and And solve the problems, such as the unstable explosive of hydrogen, when needing hydrogen feed, by control button electric hydaulic can be controlled to push away Bar opens the first valve, takes out the lanthanum nickel metal derby inside storage box, it is slightly heated, lanthanum nickel metal derby just can be by hydrogen It releases again, starts return pump after the completion of Hydrogen collection, then by control button, the nitrogen in separator box is passed through into nitrogen Conduit is pumped into collecting box and stores, for preparing the raw material of liquefied ammonia in the future.
Description of the drawings
Attached drawing is used to provide a further understanding of the present invention, and a part for constitution instruction, with this practicality New embodiment for explaining the utility model, does not form the limitation to the utility model together.In the accompanying drawings:
Fig. 1 is the overall structure diagram of the utility model;
Fig. 2 is the decomposition tank internal structure schematic diagram of the utility model;
In figure:1- material taking mouths;2- control panels;3- control buttons;4- decomposes tank;5- liquefied ammonia entrances;6- nitrogen conduits;7- Case lid;8- collecting boxs;The first valves of 9-;10- electric drive hydraulic thrusters;11- lanthanum nickel metal derbies;12- purifies case;13- adsorbents; 14- heaters;15- separator boxs;16- gas separation membranes;17- pneumohydraulic pressure-cylinders;18- heater boxes;19- catalyst nozzles;20- rings Shape water pipe;21- storage boxes;22- electric pushrods;The second valves of 23-;24- return pumps;25- airflow ducts;26- electrothermal tubes.
Specific embodiment
The following is a combination of the drawings in the embodiments of the present utility model, and the technical scheme in the embodiment of the utility model is carried out It clearly and completely describes, it is clear that the described embodiments are only a part of the embodiments of the utility model rather than whole Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are without making creative work All other embodiments obtained shall fall within the protection scope of the present invention.
- 2 are please referred to Fig.1, the utility model provides a kind of technical solution:Automatic control structure raw material decomposes device, including Material taking mouth 1, control panel 2, control button 3, decomposition tank 4, liquefied ammonia entrance 5, nitrogen conduit 6, case lid 7, collecting box 8, the first valve Door 9, electric drive hydraulic thruster 10, lanthanum nickel metal derby 11, purification case 12, adsorbent 13, heater 14, separator box 15, gas separation Film 16, pneumohydraulic pressure-cylinder 17, heater box 18, catalyst nozzle 19, annular conduit 20, storage box 21, electric pushrod 22, the second valve Door 23, return pump 24, airflow duct 25 and electrothermal tube 26, the top for decomposing tank 4 offer material taking mouth 1, the one side peace of material taking mouth 1 Equipped with control panel 2, the one side of control panel 2 is equipped with control button 3, and the one side of control button 3 offers liquefied ammonia entrance 5, The one side of liquefied ammonia entrance 5 is equipped with nitrogen conduit 6, and the one side of nitrogen conduit 6 is equipped with collecting box 8, the one side installation of collecting box 8 There is case lid 7, the inside for decomposing tank 4 is equipped with heater box 18, and the inside of heater box 18 is equipped with electrothermal tube 26, the table of electrothermal tube 26 Face is wound with annular conduit 20, and the inside of annular conduit 20 is equipped with catalyst nozzle 19, and heater box 18 passes through airflow duct 25 It is connected with separator box 15, the inside of separator box 15 is equipped with pneumohydraulic pressure-cylinder 17, and the one side of pneumohydraulic pressure-cylinder 17 is equipped with evacuation Pump 24, the one side of return pump 24 are equipped with gas separation membrane 16, and separator box 15 is connected with purification case 12 by airflow duct 25, carried The inside installation having heaters 14 of pure case 12, the inner wall insertion of purification case 12 are equipped with adsorbent 13, and purification case 12 passes through air-flow Conduit 25 is connected with storage box 21, and the inside of storage box 21 is equipped with the second valve 23, and the one side of the second valve 23 is equipped with electricity Dynamic push rod 22, the one side of electric pushrod 22 are equipped with lanthanum nickel metal derby 11, and the one side of lanthanum nickel metal derby 11 is equipped with the first valve 9, the one side of the first valve 9 is equipped with electric drive hydraulic thruster 10, and control panel 2 is electrically connected electric drive hydraulic thruster 10, electronic pushes away Bar 22 and return pump 24.
Further, annular conduit 20 is connected by ring flange with decomposing the one side inner wall of tank 4, and connection is simple secured.
Further, electric drive hydraulic thruster 10 is connected by screw with decomposing the one side inner wall of tank 4, assembling easy to disassemble.
Further, the first valve 9 is connected by slide with storage box 21, is conducive to moving left and right for the first valve 9.
Operation principle:During using the device, 3 starter of control button is first passed through, then liquid ammonia is passed through into liquefied ammonia entrance 5 It pours into annular conduit 20, since annular conduit 20 is wound around the surface of electrothermal tube 26, liquid ammonia can be with uniform speed slow Flow through annular conduit 20, it is fully heated convenient for liquid ammonia, while the catalyst nozzle 19 inside annular conduit 20 can be sprayed and urged Agent, liquid ammonia can resolve into nitrogen, hydrogen and a small amount of steam under the action of high mild catalytic, due to nitrogen and hydrogen During density is less than air, therefore two kinds of mixed gas can be along airflow duct 25 into separator box 15, the gas inside separator box 15 Liquid pressurized cylinder 17 can increase the pressure inside separator box 15 so that the permeability of gas separation membrane 16 changes, so that hydrogen Gas can be by gas separation membrane 16, and nitrogen is then left in separator box 15, and the hydrogen after separation continues on airflow duct 25 into purification case 12, still containing a small amount of nitrogen and steam, after purification case 12 is entered, heater 14 in the hydrogen after decomposition Work so that the adsorbent 13 inside purification case 12 fully absorbs nitrogen and steam in hydrogen, further obtains more pure Hydrogen, after purification, then electric pushrod 22 is started by control button 3 and opens the second valve 23 so that hydrogen enters storage In case 21, the lanthanum nickel metal derby 11 inside storage box 21 can be good at absorption of hydrogen and be stored up, and solve hydrogen The problem of gas unstable explosive, when needing hydrogen feed, can control electric drive hydraulic thruster 10 by first by control button 3 Valve 9 is opened, and is taken out the lanthanum nickel metal derby 11 inside storage box 21, it is slightly heated, lanthanum nickel metal derby 11 just can be by hydrogen It releases again, starts return pump 24 after the completion of Hydrogen collection, then by control button 3, the nitrogen in separator box 15 is led to It crosses in the suction collecting box 8 of nitrogen conduit 6 and stores, for preparing the raw material of liquefied ammonia in the future.
Finally it should be noted that:The above is only the preferred embodiment of the utility model only, is not limited to this Utility model, although the utility model is described in detail with reference to the foregoing embodiments, for those skilled in the art For, it can still modify to the technical solution recorded in foregoing embodiments or to which part technical characteristic Carry out equivalent substitution.Within the spirit and principle of the utility model, any modifications, equivalent replacements and improvements are made, It should be included within the scope of protection of this utility model.

Claims (4)

1. automatic control structure raw material decomposes device, including material taking mouth (1), control panel (2), control button (3), decomposition tank (4), liquefied ammonia entrance (5), nitrogen conduit (6), case lid (7), collecting box (8), the first valve (9), electric drive hydraulic thruster (10), lanthanum Nickel metal derby (11), purification case (12), adsorbent (13), heater (14), separator box (15), gas separation membrane (16), gas-liquid Pressurized cylinder (17), heater box (18), catalyst nozzle (19), annular conduit (20), storage box (21), electric pushrod (22), Two valves (23), return pump (24), airflow duct (25) and electrothermal tube (26), it is characterised in that:The top for decomposing tank (4) Material taking mouth (1) is offered, the one side of the material taking mouth (1) is equipped with control panel (2), the one side peace of the control panel (2) Equipped with control button (3), the one side of the control button (3) offers liquefied ammonia entrance (5), the one side of the liquefied ammonia entrance (5) Nitrogen conduit (6) is installed, the one side of the nitrogen conduit (6) is equipped with collecting box (8), the one side peace of the collecting box (8) Equipped with case lid (7), the inside for decomposing tank (4) is equipped with heater box (18), and the inside of the heater box (18) is equipped with electricity Heat pipe (26), the surface wrap of the electrothermal tube (26) have annular conduit (20), and the inside of the annular conduit (20) is equipped with Catalyst nozzle (19), the heater box (18) are connected by airflow duct (25) with separator box (15), the separator box (15) Inside pneumohydraulic pressure-cylinder (17) is installed, the one side of the pneumohydraulic pressure-cylinder (17) is equipped with return pump (24), the evacuation The one side of pump (24) is equipped with gas separation membrane (16), and the separator box (15) is connected by airflow duct (25) and purification case (12) It connects, the inside installation having heaters (14) of the purification case (12), the inner wall insertion of the purification case (12) is equipped with adsorbent (13), the purification case (12) is connected by airflow duct (25) with storage box (21), the inside installation of the storage box (21) There is the second valve (23), the one side of second valve (23) is equipped with electric pushrod (22), and the one of the electric pushrod (22) Side is equipped with lanthanum nickel metal derby (11), and the one side of the lanthanum nickel metal derby (11) is equipped with the first valve (9), first valve (9) one side is equipped with electric drive hydraulic thruster (10), and the control panel (2) is electrically connected electric drive hydraulic thruster (10), electronic Push rod (22) and return pump (24).
2. automatic control structure raw material decomposes device according to claim 1, it is characterised in that:The annular conduit (20) It is connected by ring flange with decomposing the one side inner wall of tank (4).
3. automatic control structure raw material decomposes device according to claim 1, it is characterised in that:The electric drive hydraulic thruster (10) it is connected by screw with decomposing the one side inner wall of tank (4).
4. automatic control structure raw material decomposes device according to claim 1, it is characterised in that:First valve (9) It is connected by slide with storage box (21).
CN201721351668.6U 2017-10-19 2017-10-19 Automatic control structure raw material decomposes device Expired - Fee Related CN207385424U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721351668.6U CN207385424U (en) 2017-10-19 2017-10-19 Automatic control structure raw material decomposes device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721351668.6U CN207385424U (en) 2017-10-19 2017-10-19 Automatic control structure raw material decomposes device

Publications (1)

Publication Number Publication Date
CN207385424U true CN207385424U (en) 2018-05-22

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Application Number Title Priority Date Filing Date
CN201721351668.6U Expired - Fee Related CN207385424U (en) 2017-10-19 2017-10-19 Automatic control structure raw material decomposes device

Country Status (1)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112657448A (en) * 2020-12-17 2021-04-16 湖北朗昕生化药业有限公司 Sodium triacetoxyborohydride production device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112657448A (en) * 2020-12-17 2021-04-16 湖北朗昕生化药业有限公司 Sodium triacetoxyborohydride production device

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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: 20180522

Termination date: 20181019