CN113735632B - A magnetron air plasma preparation system for nitrogen fertilizer - Google Patents

A magnetron air plasma preparation system for nitrogen fertilizer Download PDF

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CN113735632B
CN113735632B CN202111029952.2A CN202111029952A CN113735632B CN 113735632 B CN113735632 B CN 113735632B CN 202111029952 A CN202111029952 A CN 202111029952A CN 113735632 B CN113735632 B CN 113735632B
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plasma reaction
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CN113735632A (en
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宋一嘉
熊青
杨琦
乔俊杰
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Chongqing University
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    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05CNITROGENOUS FERTILISERS
    • C05C1/00Ammonium nitrate fertilisers
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    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B21/00Nitrogen; Compounds thereof
    • C01B21/20Nitrogen oxides; Oxyacids of nitrogen; Salts thereof
    • C01B21/38Nitric acid
    • C01B21/40Preparation by absorption of oxides of nitrogen
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
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Abstract

The invention discloses a magnetic control type system for preparing nitrogen fertilizer by air plasma, which comprises a solar power generation device, a magnetic field control device, a plasma reaction device, an oxidation cavity device and a gas absorption pool device, wherein the magnetic field control device is connected with the solar power generation device, the solar power generation device supplies clean electric energy for the magnetic field control device, and the high-voltage end of the plasma reaction device is connected with the solar power generation device. The invention takes air as raw material, and effectively improves the yield of nitrogen oxide generated by plasma by combining magnetic field control and a variable diameter air flow field; converting nitrogen in the air into nitric oxide, further converting the nitric oxide into nitric acid molecules, and combining free ammonia in the agricultural fertilizer to generate stable and easily absorbed ammonium nitrate so as to improve the property of the agricultural fertilizer and serve as a nitrogen fertilizer for crop growth; the equipment is simple and portable, is beneficial to the rural area to use the air temperature plasma for carrying out autonomous nitrogen fixation and fertilizer preparation in a large range, and the reactants are green and pollution-free.

Description

一种磁控式空气等离子体制备氮肥系统A magnetron air plasma preparation system for nitrogen fertilizer

技术领域technical field

本发明涉及氮肥制备技术领域,具体为一种磁控式空气等离子体制备氮肥系统。The invention relates to the technical field of nitrogen fertilizer preparation, in particular to a magnetron air plasma preparation system for nitrogen fertilizer.

背景技术Background technique

诞生于19世纪的哈伯-博施法是目前工业上应用最为广泛的,产量最大的人工固氮方法,每年可生产约1.4亿吨氮气,超过了农业生产固氮的总量,维持着地球40%人口的温饱,是现代农业的基础。然而,哈伯法固氮产业每年能量消耗占全球能量总消耗的2%,天然气总消耗的5%,且排放超过3亿吨二氧化碳,能耗极高、碳排放极大,严重影响全球生态环境。此外,哈伯法合成的铵盐,不仅有效期短、施肥后往往有相当一部分肥料会形成极易挥发的氨气从土壤中逸出,大大降低了氮肥的有效性和利用率,导致农业生产成本尤其是化肥成本居高不下。The Haber-Bosch method, which was born in the 19th century, is currently the most widely used and most productive artificial nitrogen fixation method in industry. It can produce about 140 million tons of nitrogen per year, exceeding the total amount of nitrogen fixed by agricultural production and maintaining 40% of the earth's population. food and clothing is the foundation of modern agriculture. However, the annual energy consumption of the Haber nitrogen fixation industry accounts for 2% of the total global energy consumption, 5% of the total natural gas consumption, and emits more than 300 million tons of carbon dioxide. The energy consumption and carbon emissions are extremely high, which seriously affects the global ecological environment. In addition, the ammonium salt synthesized by the Haber method not only has a short period of validity, but also a considerable part of the fertilizer will form highly volatile ammonia gas and escape from the soil after fertilization, which greatly reduces the effectiveness and utilization rate of nitrogen fertilizer, resulting in agricultural production costs. In particular, the cost of fertilizers remains high.

另一方面,随着人口爆发式增长及三次工业革命的推进,固氮需求尤其是农业用氮肥需求量越来越高。由于氮肥是所有农业产品生产的必需品,而铵盐、硝酸盐又是化工、有色冶金等工业的基础,因此全世界对于含氮化合物尤其是氮肥的需求量与日俱增,工业固氮占比也越来越大。On the other hand, with the explosive growth of population and the advancement of the three industrial revolutions, the demand for nitrogen fixation, especially for agricultural nitrogen fertilizers, is getting higher and higher. Since nitrogen fertilizer is a necessity for the production of all agricultural products, and ammonium salts and nitrates are the basis of chemical industry, non-ferrous metallurgy and other industries, the world's demand for nitrogen-containing compounds, especially nitrogen fertilizers, is increasing day by day, and the proportion of industrial nitrogen fixation is also increasing. big.

近年来,随着新能源发电以及等离子体技术的深入研究,人工固氮技术也得到了新发展。等离子体固氮技术是一种清洁无碳排放、常温常压、易操作的新兴人工固氮工艺。其通过高压击穿放电产生的等离子体与空气作用,将空气中的氮气和氧气转化合成氮氧化物。等离子体固氮技术所需原料为空气,充足且极易获得,生成的氮氧化物溶于水后形成的硝酸(HNO3)可降低含氮有机农肥的pH值,将挥发性的氨气转化为稳定的硝酸铵(NH4NO3),使得农肥中氮含量翻倍,经济价值极高。该方法极大地避免了传统工业固氮方法所存在的碳排放大等环境污染问题,为人工固氮技术的发展提供了新方向。In recent years, with the in-depth research of new energy power generation and plasma technology, artificial nitrogen fixation technology has also been newly developed. Plasma nitrogen fixation technology is an emerging artificial nitrogen fixation process that is clean, carbon-free, normal temperature and pressure, and easy to operate. It converts nitrogen and oxygen in the air into nitrogen oxides through the action of plasma generated by high-voltage breakdown discharge and air. The raw material required for the plasma nitrogen fixation technology is air, which is sufficient and easy to obtain. Nitric acid (HNO3) formed after the nitrogen oxides are dissolved in water can reduce the pH value of nitrogen-containing organic fertilizers and convert volatile ammonia gas into stable The amount of ammonium nitrate (NH4NO3) doubles the nitrogen content in agricultural fertilizers and is of extremely high economic value. This method greatly avoids the environmental pollution problems such as large carbon emissions existing in traditional industrial nitrogen fixation methods, and provides a new direction for the development of artificial nitrogen fixation technology.

发明内容SUMMARY OF THE INVENTION

本发明的目的在于提供一种磁控式空气等离子体制备氮肥系统,利用大气压空气直流辉光放电形成高稳定性等离子体,结合磁场控制,扩大等离子体区域的体积,增大了等离子体与空气的作用区域,解决了等离子体固氮过程中氮氧化物合成效率低的问题。大量氮氧化物经由大气压或者高气压空气条件下氧化,并排入吸收池形成硝酸溶液,硝酸与有机农肥中游离态的氨发生化学反应,生成稳定的硝酸铵肥料,有效提高农肥中可被植物吸收的氮含量。The purpose of the present invention is to provide a magnetron-type air plasma preparation system for nitrogen fertilizer, which utilizes atmospheric pressure air DC glow discharge to form high-stability plasma, combined with magnetic field control, expands the volume of the plasma area, and increases the amount of plasma and air It can solve the problem of low synthesis efficiency of nitrogen oxides in the process of plasma nitrogen fixation. A large amount of nitrogen oxides are oxidized under atmospheric pressure or high-pressure air, and discharged into the absorption tank to form a nitric acid solution. The nitric acid chemically reacts with the free ammonia in the organic fertilizer to generate a stable ammonium nitrate fertilizer, which effectively improves the ability of the fertilizer to be absorbed by plants. nitrogen content.

Figure BDA0003244674400000021
Figure BDA0003244674400000021

HNO3+NH3→NH4NO3 HNO 3 +NH 3 →NH 4 NO 3

上述通过增加氮氧化物产率提高固氮率的目标是通过以下技术方案来实现的:一种磁控式空气等离子体制备氮肥系统,其中,包括太阳能发电装置、磁场控制装置、等离子体反应装置、氧化腔体装置和气体吸收池装置,所述磁场控制装置连接太阳能发电装置,所述太阳能发电装置为磁场控制装置供给清洁电能,所述等离子体反应装置高压端与太阳能发电装置相连接,所述氧化腔体装置进气口连接等离子体反应装置,所述氧化腔体装置出气口与气体吸收池装置经由管道相连,形成氮氧化物向硝酸铵转化的通道。The above goal of improving nitrogen fixation rate by increasing nitrogen oxide yield is achieved through the following technical solutions: a magnetron air plasma preparation system for nitrogen fertilizer, which includes a solar power generation device, a magnetic field control device, a plasma reaction device, an oxidation A cavity device and a gas absorption cell device, the magnetic field control device is connected to a solar power generation device, the solar power generation device supplies clean electric energy to the magnetic field control device, the high-voltage end of the plasma reaction device is connected to the solar power generation device, the oxidation The air inlet of the cavity device is connected to the plasma reaction device, and the air outlet of the oxidation chamber device is connected to the gas absorption pool device through a pipeline to form a channel for the conversion of nitrogen oxides to ammonium nitrate.

优选的,所述太阳能发电装置包括光伏太阳能板、蓄电池、脉冲发生器模块、百毫安直流电源模块、安培量级直流电源模块,所述光伏太阳能板连接蓄电池,所述脉冲发生器模块连接等离子体反应装置,所述百毫安直流电源模块连接等离子体反应装置,所述安培量级直流电源模块连接磁场控制装置。Preferably, the solar power generation device includes a photovoltaic solar panel, a battery, a pulse generator module, a 100 mA DC power supply module, and an ampere-level DC power supply module, the photovoltaic solar panel is connected to the storage battery, and the pulse generator module is connected to the plasma The body reaction device, the 100 mA DC power module is connected to the plasma reaction device, and the ampere-level DC power module is connected to the magnetic field control device.

优选的,所述磁场控制装置包括载流螺线管、圆环磁芯,所述载流螺线管一端连接安培量级直流电源模块,所述载流螺线管通电产生磁场,所述磁场控制装置为采取M×N形式阵列的多组,多组所述磁场控制装置之间经由导线联通。Preferably, the magnetic field control device includes a current-carrying solenoid and a toroidal magnetic core, one end of the current-carrying solenoid is connected to an ampere-level DC power supply module, the current-carrying solenoid is energized to generate a magnetic field, and the magnetic field is The control devices are multiple groups of arrays in the form of M×N, and the multiple groups of the magnetic field control devices are communicated via wires.

优选的,所述等离子体反应装置包括钨棒电极、金属管电极、介质管、位移控制平台,所述金属管电极连接脉冲发生器模块、百毫安直流电源模块的正极,所述钨棒电极接地、并下端连接位移控制平台,所述位移控制平台用于调节钨棒电极位置,所述金属管电极置于介质管上端,与介质管贴合,所述介质管下方的两侧设有两个进气口,所述等离子体反应装置与磁场控制装置采取相同阵列形式,所述金属管电极的底部为放电区域,所述圆环磁芯置于介质管与载流螺线管之间。Preferably, the plasma reaction device includes a tungsten rod electrode, a metal tube electrode, a medium tube, and a displacement control platform. Grounded and connected to the displacement control platform at the lower end. The displacement control platform is used to adjust the position of the tungsten rod electrode. The metal tube electrode is placed on the upper end of the medium tube and is attached to the medium tube. Two sides are provided below the medium tube. The plasma reaction device and the magnetic field control device take the same array form, the bottom of the metal tube electrode is a discharge area, and the annular magnetic core is placed between the dielectric tube and the current-carrying solenoid.

优选的,所述氧化腔体装置包括氧化腔室、气泵、控制阀,所述气泵连接等离子体反应装置,所述控制阀设置在氧化腔体装置的进气端口和出气端口。Preferably, the oxidation chamber device includes an oxidation chamber, an air pump, and a control valve, the air pump is connected to the plasma reaction device, and the control valve is provided at the air inlet port and the air outlet port of the oxidation chamber device.

优选的,所述气体吸收池装置包括一级吸收池、二级吸收池、水泵,所述一级吸收池经由管道连接氧化腔体装置的出气口,将氧化后的氮氧化物溶入溶液中变成硝酸溶液,所述二级吸收池连接一级吸收池,接收一级吸收池中的硝酸溶液,硝酸溶液捕获二级吸收池中的游离态氨。Preferably, the gas absorption pool device includes a primary absorption pool, a secondary absorption pool, and a water pump, and the primary absorption pool is connected to the gas outlet of the oxidation chamber device through a pipeline, and the oxidized nitrogen oxides are dissolved into the solution It becomes a nitric acid solution, the secondary absorption tank is connected to the primary absorption tank, receives the nitric acid solution in the primary absorption tank, and the nitric acid solution captures the free ammonia in the secondary absorption tank.

优选的,所述介质管为变径介质管,所述介质管靠近放电区域的一侧为空心的锥形,所述介质管的底部为空心的圆柱形。Preferably, the medium pipe is a variable diameter medium pipe, the side of the medium pipe close to the discharge area is a hollow cone, and the bottom of the medium pipe is a hollow cylinder.

优选的,所述等离子体反应装置中的上下电极采取棒-棒形式或管-棒形式。Preferably, the upper and lower electrodes in the plasma reaction device take a rod-rod form or a tube-rod form.

与现有技术相比,本发明的有益效果是:Compared with the prior art, the beneficial effects of the present invention are:

该磁控式空气等离子体制备氮肥系统,以空气作为原材料,通过结合磁场控制和变径空气流场有效地提高等离子体生成的氮氧化物产率;将农作物无法直接利用的空气中氮元素结合农肥中游离态氨生产出稳定易吸收的硝酸铵,有效改善了农肥性质;设备简易轻便,有利于农村地区大范围使用空气温等离子体进行自主固氮制肥;等离子体反应装置由太阳能作为供给电源,反应物绿色无污染,实现碳的“零排放”,契合绿色发展的新理念。The magnetron air plasma preparation nitrogen fertilizer system uses air as a raw material, and effectively improves the yield of nitrogen oxides generated by plasma by combining magnetic field control and variable diameter air flow field; the nitrogen in the air that cannot be directly used by crops is combined with agricultural fertilizers The neutral free ammonia produces stable and easily absorbed ammonium nitrate, which effectively improves the properties of agricultural fertilizers; the equipment is simple and portable, which is conducive to the use of air-temperature plasma in rural areas for autonomous nitrogen fixation and fertilizer production; the plasma reaction device uses solar energy as the power supply to react It is green and pollution-free, and realizes "zero emission" of carbon, which is in line with the new concept of green development.

附图说明Description of drawings

图1为一种磁控式空气等离子体制备氮肥系统的系统示意图;Fig. 1 is a system schematic diagram of a magnetron air plasma preparation system for nitrogen fertilizer;

图2为一种磁控式空气等离子体制备氮肥系统的等离子体反应装置工作示意图。FIG. 2 is a schematic working diagram of a plasma reaction device of a magnetron air plasma preparation system for nitrogen fertilizer.

图中:1、太阳能发电装置;2、磁场控制装置;3、等离子体反应装置;4、氧化腔体装置;5、气体吸收池装置;6、光伏太阳能板;7、蓄电池;8、脉冲发生器模块;9、百毫安直流电源模块;10、安培量级直流电源模块;11、载流螺线管;12、圆环磁芯;13、钨棒电极;14、金属管电极;15、介质管;16、位移控制平台;17、氧化腔室;18、气泵;19、控制阀;20、一级吸收池;21、二级吸收池;22、水泵;23、放电区域。In the figure: 1. Solar power generation device; 2. Magnetic field control device; 3. Plasma reaction device; 4. Oxidation cavity device; 5. Gas absorption cell device; 6. Photovoltaic solar panel; 7. Battery; 8. Pulse generation 9. 100mA DC power supply module; 10. Ampere level DC power supply module; 11. Current-carrying solenoid; 12. Ring magnetic core; 13. Tungsten rod electrode; 14. Metal tube electrode; 15. 16. Displacement control platform; 17. Oxidation chamber; 18. Air pump; 19. Control valve; 20. Primary absorption pool; 21. Secondary absorption pool; 22. Water pump;

具体实施方式Detailed ways

下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, but not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.

以下结合图1,图2来对本发明的具体实施方式作进一步的阐述。本发明中,一种磁控式空气等离子体制备氮肥系统,包括太阳能发电装置1、磁场控制装置2、等离子体反应装置3、氧化腔体装置4和气体吸收池装置5,磁场控制装置2连接太阳能发电装置1,太阳能发电装置1为磁场控制装置2供给清洁电能,等离子体反应装置3高压端与太阳能发电装置1相连接,氧化腔体装置4进气口连接等离子体反应装置3,氧化腔体装置4出气口与气体吸收池装置5经由管道相连,形成氮氧化物向硝酸铵转化的通道;The specific embodiments of the present invention will be further described below with reference to FIG. 1 and FIG. 2 . In the present invention, a magnetron air plasma preparation system for nitrogen fertilizer includes a solar power generation device 1, a magnetic field control device 2, a plasma reaction device 3, an oxidation cavity device 4 and a gas absorption cell device 5, and the magnetic field control device 2 is connected to Solar power generation device 1, solar power generation device 1 supplies clean electric power to magnetic field control device 2, plasma reaction device 3 is connected to the high voltage end of solar power generation device 1, oxidation chamber device 4 The air inlet is connected to plasma reaction device 3, oxidation chamber The gas outlet of the body device 4 is connected with the gas absorption tank device 5 via a pipeline to form a channel for the conversion of nitrogen oxides to ammonium nitrate;

太阳能发电装置1包括光伏太阳能板6、蓄电池7、脉冲发生器模块8、百毫安直流电源模块9、安培量级直流电源模块10,光伏太阳能板6连接蓄电池7,将太阳能转化成电能储存,作为磁控式空气等离子体制备氮肥系统的能量源;脉冲发生器模块8连接等离子体反应装置3,是放电等离子体的点火装置;百毫安直流电源模块9连接等离子体反应装置3,用于维持空气等离子体;安培量级直流电源模块10连接磁场控制装置2,用于产生及调节磁场。The solar power generation device 1 includes a photovoltaic solar panel 6, a storage battery 7, a pulse generator module 8, a 100 mA DC power supply module 9, and an ampere-level DC power supply module 10. The photovoltaic solar panel 6 is connected to the storage battery 7, and converts solar energy into electrical energy for storage. As the energy source of the magnetron air plasma preparation system for nitrogen fertilizer; the pulse generator module 8 is connected to the plasma reaction device 3 and is the ignition device of the discharge plasma; the 100mA DC power supply module 9 is connected to the plasma reaction device 3 and is used for Air plasma is maintained; the ampere-level DC power supply module 10 is connected to the magnetic field control device 2 for generating and adjusting the magnetic field.

磁场控制装置2包括载流螺线管11、圆环磁芯12,载流螺线管11一端连接安培量级直流电源模块10,通电载流螺线管11将产生磁场(磁场方向为竖直方向,由上至下或由下至上均可),控制等离子体分布区域,增加与空气的作用面积;磁场控制装置2为采取M×N形式阵列的多组,多组磁场控制装置2之间经由导线联通。The magnetic field control device 2 includes a current-carrying solenoid 11 and an annular magnetic core 12. One end of the current-carrying solenoid 11 is connected to the ampere-level DC power supply module 10, and the current-carrying solenoid 11 is energized to generate a magnetic field (the direction of the magnetic field is vertical). direction, from top to bottom or bottom to top), to control the plasma distribution area and increase the interaction area with the air; communicated via wires.

等离子体反应装置3包括钨棒电极13、金属管电极14、介质管15、位移控制平台16,金属管电极14连接脉冲发生器模块8、百毫安直流电源模块9的正极,钨棒电极13下端连接位移控制平台16;金属管电极14置于介质管15上端,与介质管15贴合,作为高压端,其中钨棒电极13和金属管电极14正负极性可换;介质管15设有两个进气口,作为气体通道以及反应容器,介质管15下端采取圆柱形或锥形管口,其中锥形管口有利于空气涌入等离子体反应装置3的放电区域23;位移控制平台16可调节钨棒电极13位置,控制放电间距,位移控制平台16可以去除,不本质影响等离子体反应装置3正常运行,等离子体反应装置3与磁场控制装置2采取相同阵列形式,两者协同使用,金属管电极14的底部为放电区域23,圆环磁芯12置于介质管15与载流螺线管11之间,用于增强磁场强度。The plasma reaction device 3 includes a tungsten rod electrode 13, a metal tube electrode 14, a medium tube 15, and a displacement control platform 16. The metal tube electrode 14 is connected to the pulse generator module 8, the positive electrode of the 100 mA DC power supply module 9, and the tungsten rod electrode 13 The lower end is connected to the displacement control platform 16; the metal tube electrode 14 is placed on the upper end of the medium tube 15, and is attached to the medium tube 15 as a high-voltage end, wherein the positive and negative polarities of the tungsten rod electrode 13 and the metal tube electrode 14 are interchangeable; the medium tube 15 is provided with There are two air inlets, which are used as gas channels and reaction vessels. The lower end of the medium tube 15 adopts a cylindrical or conical orifice, wherein the conical orifice is conducive to the influx of air into the discharge area 23 of the plasma reaction device 3; the displacement control platform 16 The position of the tungsten rod electrode 13 can be adjusted, the discharge distance can be controlled, and the displacement control platform 16 can be removed, which does not substantially affect the normal operation of the plasma reaction device 3. The plasma reaction device 3 and the magnetic field control device 2 take the same array form, and the two are used together. , the bottom of the metal tube electrode 14 is the discharge area 23, and the annular magnetic core 12 is placed between the dielectric tube 15 and the current-carrying solenoid 11 to enhance the magnetic field strength.

等离子体反应装置3中的上下电极采取棒-棒形式或管-棒形式。The upper and lower electrodes in the plasma reaction device 3 take the form of rod-rod or tube-rod.

氧化腔体装置4包括氧化腔室17、气泵18、控制阀19,气泵18连接等离子体反应装置3,在接收空气温等离子体反应阵列装置3产生氮氧化物的同时促进系统中气体的流动;控制阀19设置在氧化腔体装置4的进气端口和出气端口,用于控制系统的气体流量。The oxidation chamber device 4 includes an oxidation chamber 17, an air pump 18, and a control valve 19. The air pump 18 is connected to the plasma reaction device 3, and promotes the flow of gas in the system while receiving the air temperature plasma reaction array device 3 to generate nitrogen oxides; The control valve 19 is arranged at the inlet port and the outlet port of the oxidation chamber device 4, and is used for controlling the gas flow of the system.

气体吸收池装置5包括一级吸收池20、二级吸收池21、水泵22,一级吸收池20经由管道连接氧化腔体装置4的出气口,将氧化后的氮氧化物溶入溶液中变成硝酸溶液;二级吸收池21连接一级吸收池20,接收一级吸收池20中的硝酸溶液,硝酸溶液捕获二级吸收池21中的游离态氨,两者发生化学反应形成稳定的硝酸铵,将农作物无法直接利用的空气中氮元素转换成稳定易吸收的氮肥材料。The gas absorption tank device 5 includes a first-level absorption tank 20, a second-level absorption tank 21, and a water pump 22. The first-level absorption tank 20 is connected to the gas outlet of the oxidation chamber device 4 through a pipeline, and the oxidized nitrogen oxides are dissolved in the solution to become The secondary absorption tank 21 is connected to the primary absorption tank 20 to receive the nitric acid solution in the primary absorption tank 20, and the nitric acid solution captures the free ammonia in the secondary absorption tank 21, and the two react chemically to form stable ammonium nitrate , to convert nitrogen in the air that cannot be directly used by crops into stable and easily absorbed nitrogen fertilizer materials.

磁控式空气等离子体制备氮肥系统的工作方式说明如下:如图1,首先开启氧化腔体装置4和一级吸收池20之间的阀门,打开气泵18,使空气从介质管15两侧进气口吸入等离子体反应装置3,并向一级吸收池20方向流动,此时,开启等离子体反应装置3,生成富含一氧化氮的气体,进入氧化腔室17,在氧化腔室17中,一氧化氮与空气中的氧气充分反应,生成稳定的、易溶于水的二氧化氮,二氧化氮与空气的混合气体进入一级吸收池20,与其中的水反应,形成HNO3溶液,经与水反应之后,已不含氮氧化物的空气从一级吸收池20中排出,此时,打开一级吸收池20和二级吸收池21之间的阀门,水泵22,将一级吸收池20中的硝酸溶液抽取进入二级吸收池21,与其中富氨的农家肥反应,生成NH4NO3,最终,富含NH4NO3的农家肥从二级吸收池21中排出,即为高含氮量的氮肥。The working mode of the magnetron air plasma preparation system for nitrogen fertilizer is described as follows: as shown in Figure 1, first open the valve between the oxidation chamber device 4 and the first-stage absorption tank 20, open the air pump 18, and make the air enter from both sides of the medium pipe 15. The gas port is sucked into the plasma reaction device 3 and flows in the direction of the primary absorption cell 20. At this time, the plasma reaction device 3 is turned on to generate a gas rich in nitric oxide, which enters the oxidation chamber 17, and in the oxidation chamber 17 , nitric oxide fully reacts with the oxygen in the air to generate stable, water-soluble nitrogen dioxide, the mixed gas of nitrogen dioxide and air enters the primary absorption tank 20, and reacts with the water therein to form HNO3 solution , after reacting with water, the air without nitrogen oxides is discharged from the primary absorption pool 20. At this time, open the valve between the primary absorption pool 20 and the secondary absorption pool 21. The nitric acid solution in the absorption tank 20 is drawn into the secondary absorption tank 21, and reacts with the ammonia-rich farmyard manure to generate NH4NO3 . Finally, the farmyard manure rich in NH4NO3 is discharged from the secondary absorption tank 21 , It is a nitrogen fertilizer with a high nitrogen content.

特别地,本发明中,等离子体反应装置3工作方式作如下说明:如图1、2,在气泵18的作用下,空气从气体入口持续进入,光伏太阳能板6将太阳能转化为电能,储存于蓄电池7之中,经由脉冲发生器模块8转化高电压脉冲,施加于等离子体反应装置3中的金属管电极14或钨棒电极13之上,将空气击穿,在钨棒电极13与金属管电极14之间形成等离子体通道,此时,在百毫安直流电源模块9的作用下,钨棒电极13和金属管电极14之间的等离子体可稳定维持,并关闭脉冲发生器模块8,此时,经由安培量级直流电源模块10驱动载流螺线管11,在等离子体反应装置3轴向方向产生磁场,在磁场的作用下,钨棒电极13和金属管电极14之间的等离子体体积扩大,增大了与空气的作用体积,从而提高了氮氧化物的产率,降低了能耗,最终生成的氮氧化物气体沿金属管电极14方向流出等离子体反应装置3,进入氧化腔室17。In particular, in the present invention, the working mode of the plasma reaction device 3 is described as follows: as shown in Figures 1 and 2, under the action of the air pump 18, the air continues to enter from the gas inlet, and the photovoltaic solar panel 6 converts the solar energy into electrical energy, which is stored in the In the battery 7, a high-voltage pulse is converted through the pulse generator module 8 and applied to the metal tube electrode 14 or the tungsten rod electrode 13 in the plasma reaction device 3, and the air is broken down, and the tungsten rod electrode 13 and the metal tube A plasma channel is formed between the electrodes 14. At this time, under the action of the 100mA DC power supply module 9, the plasma between the tungsten rod electrode 13 and the metal tube electrode 14 can be stably maintained, and the pulse generator module 8 is turned off. At this time, the current-carrying solenoid 11 is driven by the ampere-level DC power supply module 10, and a magnetic field is generated in the axial direction of the plasma reaction device 3. Under the action of the magnetic field, the plasma between the tungsten rod electrode 13 and the metal tube electrode 14 is The volume of the body is enlarged, which increases the volume of interaction with air, thereby improving the yield of nitrogen oxides and reducing energy consumption. The finally generated nitrogen oxides gas flows out of the plasma reaction device 3 along the direction of the metal tube electrode 14 and enters the oxidation chamber 17.

尽管已经示出和描述了本发明的实施例,对于本领域的普通技术人员而言,可以理解在不脱离本发明的原理和精神的情况下可以对这些实施例进行多种变化、修改、替换和变型,本发明的范围由所附权利要求及其等同物限定。Although embodiments of the present invention have been shown and described, it will be understood by those skilled in the art that various changes, modifications, and substitutions can be made in these embodiments without departing from the principle and spirit of the invention and modifications, the scope of the present invention is defined by the appended claims and their equivalents.

Claims (1)

1. A magnetic control type air plasma nitrogen fertilizer preparation system is characterized in that: the device comprises a solar power generation device (1), a magnetic field control device (2), a plasma reaction device (3), an oxidation cavity device (4) and a gas absorption pool device (5), wherein the magnetic field control device (2) is connected with the solar power generation device (1), the solar power generation device (1) supplies clean electric energy for the magnetic field control device (2), the high-voltage end of the plasma reaction device (3) is connected with the solar power generation device (1), the gas inlet of the oxidation cavity device (4) is connected with the plasma reaction device (3), and the gas outlet of the oxidation cavity device (4) is connected with the gas absorption pool device (5) through a pipeline to form a channel for converting nitrogen oxides to ammonium nitrate;
the solar power generation device (1) comprises a photovoltaic solar panel (6), a storage battery (7), a pulse generator module (8), a hundred milliampere direct-current power supply module (9) and an ampere-magnitude direct-current power supply module (10), wherein the photovoltaic solar panel (6) is connected with the storage battery (7), the pulse generator module (8) is connected with a plasma reaction device (3), the hundred milliampere direct-current power supply module (9) is connected with the plasma reaction device (3), and the ampere-magnitude direct-current power supply module (10) is connected with a magnetic field control device (2); the magnetic field control device (2) comprises a current-carrying solenoid (11) and a circular magnetic core (12), one end of the current-carrying solenoid (11) is connected with an ampere-magnitude direct-current power supply module (10), the current-carrying solenoid (11) is electrified to generate a magnetic field, the magnetic field control device (2) is a plurality of groups of M x N-shaped arrays, and the plurality of groups of magnetic field control devices (2) are communicated through conducting wires;
the plasma reaction device (3) comprises a tungsten rod electrode (13), a metal tube electrode (14), a medium tube (15) and a displacement control platform (16), the metal tube electrode (14) is connected with the positive electrodes of the pulse generator module (8) and the milliampere direct-current power supply module (9), the tungsten rod electrode (13) is grounded, the lower end of the tungsten rod electrode is connected with a displacement control platform (16), the displacement control platform (16) is used for adjusting the position of the tungsten rod electrode (13), the metal tube electrode (14) is arranged at the upper end of the medium tube (15), is jointed with the medium pipe (15), two air inlets are arranged at two sides below the medium pipe (15), the plasma reaction device (3) and the magnetic field control device (2) adopt the same array form, the bottom of the metal tube electrode (14) is a discharge area (23), and the circular magnetic core (12) is arranged between the medium tube (15) and the current-carrying solenoid (11);
the oxidation cavity device (4) comprises an oxidation cavity (17), an air pump (18) and a control valve (19), wherein the air pump (18) is connected with the plasma reaction device (3), and the control valve (19) is arranged at an air inlet port and an air outlet port of the oxidation cavity device (4); the gas absorption tank device (5) comprises a primary absorption tank (20), a secondary absorption tank (21) and a water pump (22), wherein the primary absorption tank (20) is connected with an air outlet of the oxidation cavity device (4) through a pipeline to dissolve oxidized nitrogen oxides into a solution to be changed into a nitric acid solution, the secondary absorption tank (21) is connected with the primary absorption tank (20) to receive the nitric acid solution in the primary absorption tank (20), and the nitric acid solution captures free ammonia in the secondary absorption tank (21); the medium tube (15) is a variable-diameter medium tube, one side of the medium tube (15) close to the discharge area (23) is a hollow cone, and the bottom of the medium tube (15) is a hollow cylinder; the upper and lower electrodes in the plasma reaction device (3) are in a rod-rod form or a tube-rod form.
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CN114205986A (en) * 2021-12-13 2022-03-18 合肥综合性国家科学中心能源研究院(安徽省能源实验室) A kind of magnetically enhanced microwave plasma nitrogen fixation method and device
NL2032635B1 (en) * 2022-07-29 2024-02-06 Lely Patent Nv Gas scrubbing device and livestock farm equipped with such a gas scrubbing device
CN115920806A (en) * 2023-01-09 2023-04-07 华中科技大学 Ammonia gas recovery and nitrogen fertilizer preparation device and method based on low-temperature plasma
CN116438996A (en) * 2023-05-30 2023-07-18 华东交通大学 Photovoltaic energy plasma nitrogen fixation device combined with sprinkling irrigation system
KR102689019B1 (en) * 2023-11-13 2024-07-25 유병순 A high-concentration nitrogen oxide generator that generates a large amount of plasma with high concentration nitrogen oxide by increasing the atmospheric pressure even when a straight wind blows into the discharge room where thunderbolt discharge is performed

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2113509A (en) * 1981-11-20 1983-08-03 Moshe Alamaro Plasma method and apparatus for the production of compounds from gas mixtures, particularly useful for the production of nitric oxides from atmospheric air
US6322661B1 (en) * 1999-11-15 2001-11-27 Lam Research Corporation Method and apparatus for controlling the volume of a plasma
JP2012145011A (en) * 2011-01-11 2012-08-02 Daihatsu Motor Co Ltd Plasma reactor
CN103648975A (en) * 2011-05-04 2014-03-19 N2应用有限公司 Energy efficient process for producing nitrogen oxide
CN104144710A (en) * 2011-12-08 2014-11-12 N2应用有限公司 Processes and plants for reducing ammonia loss and odor from organic material or waste to the atmosphere
WO2016063302A2 (en) * 2014-10-24 2016-04-28 Swasa Agro Solutions Private Limited Process for combustion of nitrogen for fertilizer production
CN111661854A (en) * 2020-05-08 2020-09-15 浙江大学 Nitrogen oxide absorption and utilization system based on low-temperature plasma catalysis nitrogen fixation
CN112266273A (en) * 2020-10-29 2021-01-26 华中科技大学 Method and system for in-situ synthesis and application of plant nitrogen fertilizer

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2113509A (en) * 1981-11-20 1983-08-03 Moshe Alamaro Plasma method and apparatus for the production of compounds from gas mixtures, particularly useful for the production of nitric oxides from atmospheric air
US6322661B1 (en) * 1999-11-15 2001-11-27 Lam Research Corporation Method and apparatus for controlling the volume of a plasma
JP2012145011A (en) * 2011-01-11 2012-08-02 Daihatsu Motor Co Ltd Plasma reactor
CN103648975A (en) * 2011-05-04 2014-03-19 N2应用有限公司 Energy efficient process for producing nitrogen oxide
CN104144710A (en) * 2011-12-08 2014-11-12 N2应用有限公司 Processes and plants for reducing ammonia loss and odor from organic material or waste to the atmosphere
WO2016063302A2 (en) * 2014-10-24 2016-04-28 Swasa Agro Solutions Private Limited Process for combustion of nitrogen for fertilizer production
CN111661854A (en) * 2020-05-08 2020-09-15 浙江大学 Nitrogen oxide absorption and utilization system based on low-temperature plasma catalysis nitrogen fixation
CN112266273A (en) * 2020-10-29 2021-01-26 华中科技大学 Method and system for in-situ synthesis and application of plant nitrogen fertilizer

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
大气压等离子体制备超疏水表面及其防冰抑霜研究;张迅 等;《电工技术学报》;20191223;第34卷(第24期);第5289-5296页 *
氮流量对磁控溅射法制备氮化钛薄膜光学性能的影响;黄佳木 等;《光学学报》;20050917;第25卷(第9期);第1293-1296页 *

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