CN106540827A - A kind of preparation facilitiess and method of dehydrogenation - Google Patents

A kind of preparation facilitiess and method of dehydrogenation Download PDF

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Publication number
CN106540827A
CN106540827A CN201610967438.6A CN201610967438A CN106540827A CN 106540827 A CN106540827 A CN 106540827A CN 201610967438 A CN201610967438 A CN 201610967438A CN 106540827 A CN106540827 A CN 106540827A
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CN
China
Prior art keywords
copper
gas
dehydrogenation
air
gas box
Prior art date
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CN201610967438.6A
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Chinese (zh)
Inventor
闻豪
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Anqing Changhong Chemical Co Ltd
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Anqing Changhong Chemical Co Ltd
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Application filed by Anqing Changhong Chemical Co Ltd filed Critical Anqing Changhong Chemical Co Ltd
Priority to CN201610967438.6A priority Critical patent/CN106540827A/en
Publication of CN106540827A publication Critical patent/CN106540827A/en
Pending legal-status Critical Current

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05BSPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B7/00Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
    • B05B7/14Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas designed for spraying particulate materials
    • B05B7/1481Spray pistols or apparatus for discharging particulate material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/72Copper

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The present invention discloses a kind of preparation facilitiess and method of dehydrogenation, device includes eruption device, drain pipe, gas box, eruption device bottom open up circular hole, close inside gas box, in the middle part of gas box, sleeve pipe is set, drain pipe one end connection circular hole one end passes through sleeve pipe, arranges air inlet, gas outlet is opened up away from eruption device one side periphery in sleeve pipe and is arranged on gas box box body at the top of gas box;Alloy liquid is poured in eruption device, alloy liquid is flowed out from eruption device bottom Jing drain pipes, gas box air inlet connects air compressor, gas outlet forms high-speed air air-flow, copper-aluminum alloy powder is formed after the alloy liquid flowed out in drain pipe and high-speed air air flow contacts, copper-aluminum alloy powder is sprayed onto in spray room, dealuminzation after powder collection, makes the dehydrogenation.The present invention is evenly distributed with copper-aluminum alloy powder, and specific surface area of catalyst is big, and catalysis activity is high, and without metallic dust, energy consumption is low, and catalyst usage cycles can extend one times of advantage.

Description

A kind of preparation facilitiess and method of dehydrogenation
Technical field
The present invention relates to field of catalyst preparation, the preparation facilitiess and method of more particularly to a kind of dehydrogenation.
Background technology
Prepare dehydrogenation often the mixture of copper and aluminum is added in crucible and fusing is heated in prior art, so Poured in the resistant to elevated temperatures diaphragm capsule for making in advance, after alloy solution natural cooling afterwards, make albronze block, then use again Jaw crusher, gyratory crusher are crushed, and after the granule after crushing is with vibrosieve screening, dealuminzation makes dehydrogenation.
The dehydrogenation prepared using this kind of method, in albronze solution, due to the proportion of copper it is bigger than aluminum, from So stand in cooling procedure, copper can sink to solution bottom and cause albronze uneven components, so as to the micropore of the copper after dealuminzation Few, catalyst activity is low, and usage cycles are short, increases production cost;Made by alloyed powder specific surface area it is less;Naturally it is cold But the time is long, and the catalyst preparation cycle is long, commercial production high cost;The preparation of the method is first to prepare albronze ingot, then Mechanical activation comminution is carried out, its process energy consumption is increased, mechanical noise is big, while producing a large amount of metallic dusts, can also bring a part into Ferrum element in machinery so as to affect catalyst catalytic performance, reduces the performance of subsequent product in catalyst.
Therefore at present the preparation method of dehydrogenation exist that catalyst activity is low, alloyed powder specific surface area is little, The problems such as rate of temperature fall is slow, mechanical activation comminution energy consumption is big, dust is more, noise is big.
The content of the invention
For the problems referred to above, the present invention proposes a kind of preparation method of dehydrogenation, improves catalyst activity, drop Warm speed, reduces mechanical activation comminution energy consumption.
The present invention solution be:
A kind of device for preparing dehydrogenation, including eruption device, drain pipe, gas box, eruption device bottom open up circular hole, gas Closing inside box, sleeve pipe being set in the middle part of gas box, drain pipe one end connection circular hole one end passes through sleeve pipe, air inlet arranged at the top of gas box Mouthful, gas outlet being opened up away from eruption device one side periphery in sleeve pipe, gas outlet is arranged on gas box box body, and gas outlet and drain pipe are remote From eruption device side simultaneously towards spray room.
Further, facilitate pouring into for alloy liquid to divide, eruption device is open-topped arc-shaped eruption device.
Further, in order to let the liquid out, the aperture of eruption device bottom circular aperture is 2~4cm.
Further, air draught, air inlet connection air compressor are passed through in order to continual.
Further, in order that gas forms high-speed air air-flow, the hole of gas outlet between sleeve pipe and the gas box in gas outlet Footpath is 2~6mm.
A kind of method for preparing dehydrogenation, alloy liquid is poured in eruption device, and alloy liquid is from eruption device bottom Jing drain pipes flow out;Gas box air inlet connects air compressor, and gas outlet forms high-speed air air-flow;The conjunction flowed out in drain pipe Golden liquid forms copper-aluminum alloy powder with high-speed air air flow contacts, and copper-aluminum alloy powder is sprayed onto in spray room, and powder is taken off after collecting Aluminum, makes dehydrogenation.
Further, alloy is albronze.
Further, copper and aluminium mixture are added in crucible, crucible is heated to 800~1050 DEG C to copper and aluminium mixture Fusing, obtains albronze solution.
Further, in the mixed thing of copper and aluminum, the mass fraction of copper is 30%~60%.
Compared with prior art, it is an advantage of the current invention that:Albronze solution directly sprays, rapid to cool down, and copper aluminum is closed Bronze end is evenly distributed, and after dealuminzation, the micropore of copper is more, and specific surface area of catalyst is big, and catalysis activity is high, without metallic dust without production Noise, energy consumption are low, and catalyst usage cycles can extend one times.
Description of the drawings
Fig. 1 is a kind of dehydrogenation preparation facilitiess schematic diagram.
Specific embodiment
The concrete technical scheme of the present invention is further described below in conjunction with Fig. 1 and specific embodiment, in order to this area Technical staff be further understood from the present invention, and do not constitute the restriction to its right.
Embodiment 1
The copper aluminium mixture that the mass fraction of copper is 30% is added in crucible, crucible is heated to 800 DEG C and mixes to copper aluminum Compound is completely melt to form albronze liquid, above-mentioned albronze liquid poured in open-topped arc-shaped eruption device 1, 1 bottom of eruption device arranges the circular hole of 2cm, and albronze liquid is flowed out from circular hole, and Jing drain pipes 2 flow out.
Close inside gas box 3, middle part arranges sleeve pipe 7;2 one end of drain pipe connects 1 bottom circular aperture of eruption device, and one end is through set Pipe 7;Air inlet 4 is set at the top of gas box, and air inlet connection air compressor opens up aperture away from eruption device one side periphery in sleeve pipe For the gas outlet of 5mm, gas outlet is arranged on gas box box body, gas outlet 5 and drain pipe 2 are exported simultaneously away from eruption device one end Towards spray room 6.
When have continual air from air inlet 4 enter gas box 3 when, due to 5 aperture of gas outlet is less and gas box 3 inside Closing, air can spray from gas outlet 5 and form high-speed air air-flow, while the alloy liquid flowed out in drain pipe 2 is held up Alloy powder is quickly cooled to, and alloy powder is sent in spray room, dealuminzation after alloy powder in spray room is collected makes institute State dehydrogenation.
Embodiment 2
The copper aluminium mixture that the mass fraction of copper is 60% is added in crucible, crucible is heated to 1050 DEG C and mixes to copper aluminum Compound is completely melt to form albronze liquid, above-mentioned albronze liquid poured in open-topped arc-shaped eruption device 1, 1 bottom of eruption device arranges the circular hole of 4cm, and albronze liquid is flowed out from circular hole, and Jing drain pipes 2 flow out.
Close inside gas box 3, middle part arranges sleeve pipe 7;2 one end of drain pipe connects 1 bottom circular aperture of eruption device, and one end is through set Pipe 7;Air inlet 4 is set at the top of gas box, and air inlet connection air compressor opens up aperture away from eruption device one side periphery in sleeve pipe For the gas outlet of 5mm, gas outlet is arranged on gas box box body, and gas outlet 5 and drain pipe 2 are away from eruption device one end outlet court simultaneously To spray room 6.
When have continual air from air inlet 4 enter gas box 3 when, due to 5 aperture of gas outlet is less and gas box 3 inside Closing, air can spray from gas outlet 5 and form high-speed air air-flow, while the alloy liquid flowed out in drain pipe 2 is held up Alloy powder is quickly cooled to, and alloy powder is sent in spray room, dealuminzation after alloy powder in spray room is collected makes institute State dehydrogenation.
Embodiment 3
The copper aluminium mixture that the mass fraction of copper is 50% is added in crucible, crucible is heated to 900 DEG C and mixes to copper aluminum Compound is completely melt to form albronze liquid, above-mentioned albronze liquid poured in open-topped arc-shaped eruption device 1, 1 bottom of eruption device arranges the circular hole of 3cm, and albronze liquid is flowed out from circular hole, and Jing drain pipes 2 flow out.
Close inside gas box 3, middle part arranges sleeve pipe 7;2 one end of drain pipe connects 1 bottom circular aperture of eruption device, and one end is through set Pipe 7;Air inlet 4 is set at the top of gas box, and air inlet connection air compressor opens up aperture away from eruption device one side periphery in sleeve pipe For the gas outlet of 5mm, gas outlet is arranged on gas box box body, and gas outlet 5 and drain pipe 2 are away from eruption device one end outlet court simultaneously To spray room 6.
When have continual air from air inlet 4 enter gas box 3 when, due to 5 aperture of gas outlet is less and gas box 3 inside Closing, air can spray from gas outlet 5 and form high-speed air air-flow, while the alloy liquid flowed out in drain pipe 2 is held up Alloy powder is quickly cooled to, and alloy powder is sent in spray room, dealuminzation after alloy powder in spray room is collected makes institute State dehydrogenation.
Should be only presently preferred embodiments of the present invention above, not to limit the present invention, all spirit in the present invention With any modification, equivalent and the improvement made within principle etc., should be included within the scope of the present invention.

Claims (9)

1. a kind of device for preparing dehydrogenation, including eruption device, drain pipe, gas box, it is characterised in that the eruption device bottom Portion opens up circular hole, closes inside the gas box, and sleeve pipe is arranged in the middle part of the gas box, and described drain pipe one end connects the circular hole one End arranges air inlet at the top of the gas box, opens up gas outlet away from eruption device one side periphery in described sleeve pipe through described sleeve pipe, The gas outlet is arranged on the gas box box body, and the gas outlet and drain pipe are away from eruption device side simultaneously towards spray room.
2. a kind of device for preparing dehydrogenation according to claim 1, it is characterised in that the eruption device is top The arc-shaped eruption device of opening.
3. a kind of preparation method of dehydrogenation according to claim 1, it is characterised in that the eruption device bottom circle The aperture in hole is 2~4cm.
4. a kind of device for preparing dehydrogenation according to claim 1, it is characterised in that the air inlet connection is empty Air compressor.
5. a kind of device for preparing dehydrogenation according to claim 1, it is characterised in that described sleeve pipe and the gas Between box, the aperture of gas outlet is 2~6mm.
6. a kind of method that device according to claim 1 prepares dehydrogenation, it is characterised in that alloy liquid is fallen Enter in eruption device, the alloy liquid is flowed out from eruption device bottom Jing drain pipes;Gas box air inlet connects air compressor, outlet Mouth forms high-speed air air-flow;The alloy liquid flowed out in the drain pipe forms into copper aluminum with the high-speed air air flow contacts Alloy powder, the copper-aluminum alloy powder are sprayed onto in spray room, dealuminzation after powder collection, make the dehydrogenation.
7. a kind of method for preparing dehydrogenation according to claim 6, it is characterised in that the alloy is that copper aluminum is closed Gold.
8. a kind of method for preparing dehydrogenation according to claim 7, it is characterised in that copper and aluminium mixture are added Enter in crucible, crucible is heated to 800~1050 DEG C and melts to above-mentioned copper and aluminium mixture, obtains the albronze solution.
9. a kind of preparation method of dehydrogenation according to claim 8, it is characterised in that the mixed thing of the copper and aluminum The mass fraction of middle copper is 30%~60%.
CN201610967438.6A 2016-10-31 2016-10-31 A kind of preparation facilitiess and method of dehydrogenation Pending CN106540827A (en)

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Application Number Priority Date Filing Date Title
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CN106540827A true CN106540827A (en) 2017-03-29

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1911570A (en) * 2006-08-18 2007-02-14 陕西科技大学 Device for preparing metal ultrafine powder and its method
CN201399582Y (en) * 2009-04-17 2010-02-10 戴煜 Device for making raw cobalt mineral powder
CN201913250U (en) * 2011-02-23 2011-08-03 长沙骅骝冶金粉末有限公司 Gas atomization device of refractory powder
CN202701384U (en) * 2012-08-19 2013-01-30 长沙拓智金属材料科技有限责任公司 Double-layered nonrestrictive atomizing and pulverizing nozzle device for high pressure gas
CN105618773A (en) * 2016-03-21 2016-06-01 南京理工大学 Gas atomization device for preparing 3D printing metal powder

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1911570A (en) * 2006-08-18 2007-02-14 陕西科技大学 Device for preparing metal ultrafine powder and its method
CN201399582Y (en) * 2009-04-17 2010-02-10 戴煜 Device for making raw cobalt mineral powder
CN201913250U (en) * 2011-02-23 2011-08-03 长沙骅骝冶金粉末有限公司 Gas atomization device of refractory powder
CN202701384U (en) * 2012-08-19 2013-01-30 长沙拓智金属材料科技有限责任公司 Double-layered nonrestrictive atomizing and pulverizing nozzle device for high pressure gas
CN105618773A (en) * 2016-03-21 2016-06-01 南京理工大学 Gas atomization device for preparing 3D printing metal powder

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Application publication date: 20170329

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