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CN113318795B - Device and method for preparing liquid metal catalyst by plasma - Google Patents

Device and method for preparing liquid metal catalyst by plasma Download PDF

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CN113318795B
CN113318795B CN202110707566.8A CN202110707566A CN113318795B CN 113318795 B CN113318795 B CN 113318795B CN 202110707566 A CN202110707566 A CN 202110707566A CN 113318795 B CN113318795 B CN 113318795B
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electrode
metal catalyst
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CN113318795A (en
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信延彬
王嘉彬
孙冰
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Dalian Maritime University
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/34Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves ; Ionic sputtering; Flame or plasma spraying; Particle radiation
    • B01J37/349Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves ; Ionic sputtering; Flame or plasma spraying; Particle radiation making use of flames, plasmas or lasers
    • 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
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/48Silver or gold
    • B01J23/50Silver
    • 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
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/85Chromium, molybdenum or tungsten
    • B01J23/88Molybdenum
    • B01J23/883Molybdenum and nickel
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/04Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing carboxylic acids or their salts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts

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Abstract

The invention discloses a device and a method for preparing a liquid metal catalyst by using plasma, wherein the device comprises a reaction chamber and a sealing cover, and the reaction chamber and the sealing cover form a containing cavity; an aeration head, an aeration pipe and a first electrode are arranged in the accommodating cavity, an insulating sleeve is arranged in the aeration pipe, and a second electrode is arranged in the insulating sleeve; one end of the aeration pipe is provided with an aeration head, the other end of the aeration pipe is provided with a sealing plug, and the second electrode is sealed with the aeration pipe through the sealing plug. The invention can form uniform and high-density plasmas, generate a large amount of active particles in a gas phase, and introduce a liquid phase to form activated water, and can effectively increase the catalytic forming rate of the liquid metal catalyst and improve the preparation efficiency of the liquid metal catalyst through the regulation and control of the types of active substances and the reaction temperature.

Description

一种等离子体制备液体金属催化剂的装置及方法Device and method for preparing liquid metal catalyst by plasma

技术领域technical field

本发明涉及催化剂制备领域,尤其涉及一种等离子体制备液体金属催化剂的装置及方法。The invention relates to the field of catalyst preparation, in particular to a device and method for preparing a liquid metal catalyst by plasma.

背景技术Background technique

金属催化剂作为催化剂种类中极为重要的一环,在多方面影响着工业生产和人类生活,如产氢行业、化工行业、电镀行业等。传统制备金属催化剂的方法主要包括浸渍法、原子沉积法、还原法、固相熔融法等,上述方法在制备过程中工艺流程繁琐、耗时,且原料中大多包含有毒有害试剂,生产过程中对环境产生一定危害。针对上述问题,近年来高速发展的等离子体技术是一种良好的解决方法。目前等离子体制备催化剂技术主要采用射流放电、介质阻挡放电、辉光放电等制备固体催化剂,而对于液体催化剂,特别是液态两相催化剂的制备研究较少。在制备液体金属催化剂时,气液传质效率低一直是气相放电制备催化剂的瓶颈。因此,开发高效的等离子体制备催化剂技术迫在眉睫。As an extremely important part of catalysts, metal catalysts affect industrial production and human life in many ways, such as hydrogen production industry, chemical industry, electroplating industry, etc. The traditional methods of preparing metal catalysts mainly include impregnation method, atomic deposition method, reduction method, solid phase melting method, etc. The process of the above methods is cumbersome and time-consuming in the preparation process, and most of the raw materials contain toxic and harmful reagents. The environment has certain hazards. In view of the above problems, the rapid development of plasma technology in recent years is a good solution. At present, the plasma catalyst preparation technology mainly uses jet discharge, dielectric barrier discharge, glow discharge, etc. to prepare solid catalysts, but there are few studies on the preparation of liquid catalysts, especially liquid two-phase catalysts. In the preparation of liquid metal catalysts, the low efficiency of gas-liquid mass transfer has always been the bottleneck of catalyst preparation by gas-phase discharge. Therefore, it is imminent to develop efficient plasma preparation catalyst technology.

发明内容Contents of the invention

本发明提供一种等离子体制备液体金属催化剂的装置及方法,以解决制备液体金属催化剂时气液传质效率低的问题。The invention provides a device and method for preparing a liquid metal catalyst by plasma to solve the problem of low gas-liquid mass transfer efficiency when preparing the liquid metal catalyst.

为了实现上述目的,本发明的技术方案是:In order to achieve the above object, technical scheme of the present invention is:

一种等离子体制备液体金属催化剂的装置,包括:反应室和密封盖,所述反应室和密封盖构成容纳腔;所述容纳腔内设有曝气头、曝气管、第一电极以及目标金属盐溶液,所述曝气管内设有绝缘套管,所述绝缘套管内设有第二电极;A device for preparing a liquid metal catalyst by plasma, comprising: a reaction chamber and a sealing cover, the reaction chamber and the sealing cover constitute an accommodating cavity; an aeration head, an aeration tube, a first electrode and a target are arranged in the accommodating cavity metal salt solution, the aeration tube is provided with an insulating sleeve, and the insulating sleeve is provided with a second electrode;

所述曝气管一端设有曝气头,另一端设有密封塞,所述第二电极通过所述密封塞固定于所述曝气管中。进一步地,所述曝气管设有导气口。An aeration head is provided at one end of the aeration tube, and a sealing plug is provided at the other end, and the second electrode is fixed in the aeration tube through the sealing plug. Further, the aeration pipe is provided with an air guide port.

进一步地,所述曝气管上设有若干微孔,所述微孔的内径为0.2~2mm。Further, the aeration pipe is provided with several micropores, and the inner diameter of the micropores is 0.2-2 mm.

进一步地,所述第一电极一端设有紧固件,所述第一电极通过所述紧固件与所述密封盖固定,并置于目标金属盐溶液中。Further, a fastener is provided at one end of the first electrode, and the first electrode is fixed to the sealing cover through the fastener and placed in the target metal salt solution.

进一步地,所述第一电极和第二电极由不锈钢或其他导电材料制成。Further, the first electrode and the second electrode are made of stainless steel or other conductive materials.

进一步地,所述电源为脉冲、直流、交流电源中的一种。Further, the power supply is one of pulse, direct current and alternating current power.

一种利用等离子体制备液体金属催化剂的装置制备液体金属催化剂的方法,包括以下步骤:A method for preparing a liquid metal catalyst using a device for preparing a liquid metal catalyst using plasma, comprising the following steps:

步骤1:配制目标金属盐溶液,调整pH值为7~10,将配置的目标金属盐溶液置于反应室中;Step 1: Prepare the target metal salt solution, adjust the pH value to 7-10, and place the configured target metal salt solution in the reaction chamber;

步骤2:向曝气管内通入载气并密封装置,对第一电极和第二电极施加电压形成等离子体,通过控制放电电压、频率和脉宽参数中的一种或多种,使得目标金属催化剂在溶液中逐渐生成。Step 2: Introduce carrier gas into the aeration tube and seal the device, apply voltage to the first electrode and the second electrode to form plasma, and control one or more of the discharge voltage, frequency and pulse width parameters to make the target metal The catalyst is gradually formed in solution.

进一步地,步骤1中所述的目标金属盐溶液的浓度为0.1~1mol/L。Further, the concentration of the target metal salt solution in step 1 is 0.1-1 mol/L.

本发明提供的一种等离子体制备液体金属催化剂的装置及方法,利用低温等离子体产生的活性物质、温度场及强电场,提高催化剂的制备效率及催化活性;同时采用曝气及曝气管开孔的方式,提高了气液两相传质效率,有效提高液体催化剂的产率。该装置及方法克服了现有等离子体制备液体催化剂的缺点,能够实现在常压下催化剂的均匀、大量、快速制备。The invention provides a device and method for preparing a liquid metal catalyst by plasma, which utilizes the active material, temperature field and strong electric field generated by the low-temperature plasma to improve the preparation efficiency and catalytic activity of the catalyst; The way of pores improves the gas-liquid two-phase mass transfer efficiency and effectively improves the yield of liquid catalysts. The device and method overcome the shortcomings of the existing plasma preparation of liquid catalysts, and can realize uniform, large-scale and rapid preparation of catalysts under normal pressure.

附图说明Description of drawings

为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作一简单地介绍,显而易见地,下面描述中的附图是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the technical solutions in the embodiments of the present invention or the prior art, the following will briefly introduce the drawings that need to be used in the description of the embodiments or the prior art. Obviously, the accompanying drawings in the following description These are some embodiments of the present invention. Those skilled in the art can also obtain other drawings based on these drawings without creative work.

图1为本发明等离子体制备液体金属催化剂的装置结构示意图。Fig. 1 is a schematic structural diagram of a device for preparing a liquid metal catalyst by plasma in the present invention.

图中:1、第一电极,2、密封塞,3、导气口,4、曝气管,5、绝缘套管,6、曝气头,7、紧固件,8、密封盖,9、反应室,10、第二电极,11、目标金属盐溶液。In the figure: 1. First electrode, 2. Sealing plug, 3. Air guide port, 4. Aeration tube, 5. Insulating sleeve, 6. Aeration head, 7. Fastener, 8. Sealing cover, 9. Reaction chamber, 10, second electrode, 11, target metal salt solution.

具体实施方式Detailed ways

为使本发明实施例的目的、技术方案和优点更加清楚,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作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。In order to make the purpose, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below in conjunction with the drawings in the embodiments of the present invention. Obviously, the described embodiments It is a part of embodiments of the present invention, but not all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without creative efforts fall within the protection scope of the present invention.

图1为等离子体制备液体金属催化剂的装置,包括:反应室9和密封盖8,所述反应室9和密封盖8构成容纳腔;所述容纳腔内设有曝气头6、曝气管4、第一电极1以及目标金属盐溶液11,所述曝气管4内设有绝缘套管5,所述绝缘套管5内设有第二电极10;优选的,所述曝气管4与第二电极10通过绝缘套管5和合适大小的密封塞2,按照第二电极10、绝缘管5、曝气管4的顺序自内而外相连接,所述绝缘套管5内径与所述第二电极10外径相适配,曝气管4内径大于绝缘套管5外径约1~20mm;优选的,曝气管内壁与绝缘套管外壁的间距为1~5mm。Fig. 1 is the device that plasma prepares liquid metal catalyst, comprises: reaction chamber 9 and sealing cover 8, and described reaction chamber 9 and sealing cover 8 constitute accommodating cavity; Aeration head 6, aeration tube are arranged in described accommodating cavity 4. The first electrode 1 and the target metal salt solution 11, the aeration tube 4 is provided with an insulating sleeve 5, and the insulating sleeve 5 is provided with a second electrode 10; preferably, the aeration tube 4 It is connected with the second electrode 10 from the inside to the outside according to the order of the second electrode 10, the insulating tube 5 and the aeration tube 4 through the insulating sleeve 5 and the sealing plug 2 of suitable size. The inner diameter of the insulating sleeve 5 is the same as the The outer diameter of the second electrode 10 is matched, and the inner diameter of the aeration tube 4 is about 1-20 mm larger than the outer diameter of the insulating sleeve 5; preferably, the distance between the inner wall of the aeration tube and the outer wall of the insulating sleeve is 1-5 mm.

所述曝气管4一端设有曝气头6,另一端设有密封塞2,所述第二电极10置于绝缘套管5内通过所述密封塞2固定于所述曝气管4中。值得注意的是,当第一电极1和第二电极10直接暴露在反应室9内时,会形成电解反应,无法引发等离子体。One end of the aeration tube 4 is provided with an aeration head 6, and the other end is provided with a sealing plug 2, and the second electrode 10 is placed in the insulating sleeve 5 and fixed in the aeration tube 4 through the sealing plug 2 . It should be noted that when the first electrode 1 and the second electrode 10 are directly exposed to the reaction chamber 9, an electrolytic reaction will be formed, and plasma cannot be induced.

进一步地,所述曝气管4设有导气口3。通过导气口3向曝气管4内通入气体。Further, the aeration pipe 4 is provided with an air guide port 3 . Gas is passed into the aeration pipe 4 through the air guide port 3 .

进一步地,所述曝气管4上设有若干微孔,所述微孔的内径为0.2~2mm。优选的,微孔数量为4~20个;使用该装置时首先在曝气管4内通入气体,防止液体通过微孔进入绝缘套管5与第二金属电极10接触,等离子体在气相中引发,被曝气吹入液相。Further, the aeration pipe 4 is provided with several micropores, and the inner diameter of the micropores is 0.2-2mm. Preferably, the number of micropores is 4 to 20; when using the device, gas is first introduced into the aeration tube 4 to prevent liquid from entering the insulating sleeve 5 through the micropores and contacting the second metal electrode 10, and the plasma is in the gas phase Initiated, blown into the liquid phase by aeration.

进一步地,所述第一电极1一端设有紧固件7,所述第一电极1通过所述紧固件7与所述密封盖8固定。Further, a fastener 7 is provided at one end of the first electrode 1 , and the first electrode 1 is fixed to the sealing cover 8 through the fastener 7 .

进一步地,所述第一电极1和第二电极10由不锈钢或其他导电材料制成。Further, the first electrode 1 and the second electrode 10 are made of stainless steel or other conductive materials.

进一步地,所述电源为脉冲、直流、交流电源中的一种。Further, the power supply is one of pulse, direct current and alternating current power.

一种利用等离子体制备液体金属催化剂的装置制备液体金属催化剂的方法,包括以下步骤:A method for preparing a liquid metal catalyst using a device for preparing a liquid metal catalyst using plasma, comprising the following steps:

步骤1:配制目标金属盐溶液,调整pH值为7~10,将配置的目标金属盐溶液置于反应室9中;Step 1: Prepare the target metal salt solution, adjust the pH value to 7-10, and place the configured target metal salt solution in the reaction chamber 9;

步骤2:向曝气管4内通入载气并密封装置,对第一电极1和第二电极10施加电压形成等离子体,通过控制放电电压、频率和脉宽参数中的一种或多种,使得目标金属催化剂在溶液中逐渐生成。Step 2: Pass the carrier gas into the aeration tube 4 and seal the device, apply voltage to the first electrode 1 and the second electrode 10 to form plasma, and control one or more of the discharge voltage, frequency and pulse width parameters , so that the target metal catalyst is gradually generated in the solution.

进一步地,步骤1中所述的目标金属盐溶液11的浓度为0.1~1mol/L。优选的,采用弱碱溶液或强碱弱酸盐溶液调节目标金属盐溶液的pH值。Further, the concentration of the target metal salt solution 11 described in step 1 is 0.1-1 mol/L. Preferably, a weak base solution or a strong base and weak salt solution is used to adjust the pH value of the target metal salt solution.

使用该装置制备液体金属催化剂时,所述电极分别接电源高压端、接地端,且当以第一电极1接地时,可利用目标金属盐溶液直接接地进而省去曝气管4外的第一电极1,等离子体引发于绝缘套管5与曝气管4之间,当绝缘套管5有微孔时,等离子体可直接与液体接触;通过所述导气口3通气将放电产生的活性物质通过曝气头6鼓入反应液中,气体种类及流速可根据反应需求调控。气体流速的控制以流量计控制,确保通过通气产生的压力使导气管外的液体不会通过曝气头或微孔进入导气管与绝缘套管之间,而熄灭等离子体。气体种类更换通过更换目标气瓶,根据反应过程需要氧化性(选择空气、氧气等),还是还原性(选择氢气、氨气等)物质的参与而选择目标气体。具体的实施例情况如下:When using this device to prepare a liquid metal catalyst, the electrodes are respectively connected to the high-voltage end of the power supply and the ground end, and when the first electrode 1 is grounded, the target metal salt solution can be used to directly ground the first electrode outside the aeration tube 4. Electrode 1, the plasma is induced between the insulating sleeve 5 and the aeration tube 4, when the insulating sleeve 5 has micropores, the plasma can directly contact the liquid; the active material generated by the discharge will be ventilated through the gas guide port 3 The gas is blown into the reaction solution through the aeration head 6, and the gas type and flow rate can be adjusted according to the reaction requirements. The control of the gas flow rate is controlled by a flow meter to ensure that the pressure generated by the ventilation prevents the liquid outside the air guide tube from entering between the air guide tube and the insulating sleeve through the aeration head or micropores, thereby extinguishing the plasma. The type of gas is replaced by changing the target gas cylinder, and the target gas is selected according to the participation of oxidizing (choose air, oxygen, etc.) or reducing (choose hydrogen, ammonia, etc.) substances in the reaction process. Concrete embodiment situation is as follows:

实施例一,将摩尔比1:1的草酸和硝酸镍用水溶解,并利用碳酸钾调整溶液pH值为10作为制备催化剂的反应液,以交流源放电,放电过程中通氧气,氧气流速为200mL/min。当放电电压5kV,放电频率3kHz,放电时间20min时,可明显看到溶液分层,分别得到油溶性草酸镍催化剂,及富含活性氧组分的水溶性催化剂。将得到的油溶性、水溶性催化剂以体积比3:1用于稠油催化改质中,其中在20℃下稠油的粘度为2016.66mPa·s。通过实验结果表明,当反应温度为290℃,反应时间为24h,稠油的粘度为403.33mPa·s,降粘率达到了80%,胶质、沥青质含量显著降低。Example 1, dissolve oxalic acid and nickel nitrate with a molar ratio of 1:1 in water, and use potassium carbonate to adjust the pH value of the solution to 10 as the reaction solution for preparing the catalyst, discharge it with an AC source, pass oxygen during the discharge process, and the oxygen flow rate is 200mL /min. When the discharge voltage is 5kV, the discharge frequency is 3kHz, and the discharge time is 20min, the solution can be clearly separated into layers, and an oil-soluble nickel oxalate catalyst and a water-soluble catalyst rich in active oxygen components can be obtained respectively. The obtained oil-soluble and water-soluble catalysts were used in the catalytic upgrading of heavy oil at a volume ratio of 3:1, where the viscosity of the heavy oil at 20°C was 2016.66 mPa·s. The experimental results show that when the reaction temperature is 290°C and the reaction time is 24 hours, the viscosity of the heavy oil is 403.33mPa·s, the viscosity reduction rate reaches 80%, and the colloid and asphaltene content are significantly reduced.

实施例二,将摩尔比1:7的七钼酸铵和硝酸镍用水溶解,加入油酸并利用氢氧化铵调整溶液pH值为8作为制备催化剂的反应液,以脉冲源放电,放电过程中通空气,空气流速为500mL/min。当峰值电压25kV,放电频率5kHz,脉宽10μs,放电时间15min时,可得到富含活性氧成分的钼酸镍双金属催化剂。将制备的催化剂用于稠油催化改质中,实验结果表明,反应温度290℃,反应时间24h,降粘率达90%,API度增加5.2。Example 2, dissolving ammonium heptamolybdate and nickel nitrate with a molar ratio of 1:7 in water, adding oleic acid and using ammonium hydroxide to adjust the pH value of the solution to 8 as the reaction solution for preparing the catalyst, discharging with a pulse source, during the discharge process Ventilate the air, the air flow rate is 500mL/min. When the peak voltage is 25kV, the discharge frequency is 5kHz, the pulse width is 10μs, and the discharge time is 15min, a nickel molybdate bimetallic catalyst rich in active oxygen components can be obtained. The prepared catalyst is used in the catalytic upgrading of heavy oil. The experimental results show that the reaction temperature is 290°C, the reaction time is 24 hours, the viscosity reduction rate reaches 90%, and the API degree increases by 5.2.

实施例三,采用1mol/L硝酸银溶液,控制pH值为7,以直流源放电,曝气管开设8个孔径为0.5mm的微孔,并以流量150mL/min的氢气作为载气制备液态纳米银催化剂。当放电电压2kV,放电时间30min,可得到粒径5~30nm的纳米银催化剂。Embodiment three, adopt 1mol/L silver nitrate solution, control pH value to be 7, discharge with direct current source, open 8 micropores that diameter is 0.5mm in aeration pipe, and prepare liquid state with the hydrogen of flow rate 150mL/min as carrier gas nanosilver catalyst. When the discharge voltage is 2kV and the discharge time is 30min, the nano-silver catalyst with a particle size of 5-30nm can be obtained.

本发明采用等离子体法制备液体金属催化剂,相对于传统催化剂制备方法,更为快速、均匀、高效,仅需数十分钟即可使催化剂大量生成;且该方法可将放电过程中产生的活性物质引入液体催化剂中,增加了催化剂的活性;此外通过放电参数调控,可有效控制催化剂的制备温度。采用该方法制备的催化剂在稠油改质等应用中具备较强的实用价值与应用前景。The invention adopts the plasma method to prepare the liquid metal catalyst. Compared with the traditional catalyst preparation method, it is more rapid, uniform and efficient, and the catalyst can be produced in a large amount in only tens of minutes; The introduction into the liquid catalyst increases the activity of the catalyst; in addition, the preparation temperature of the catalyst can be effectively controlled by adjusting the discharge parameters. The catalyst prepared by this method has strong practical value and application prospect in heavy oil upgrading and other applications.

最后应说明的是:以上各实施例仅用以说明本发明的技术方案,而非对其限制;尽管参照前述各实施例对本发明进行了详细的说明,本领域的普通技术人员应当理解:其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分或者全部技术特征进行等同替换;而这些修改或者替换,并不使相应技术方案的本质脱离本发明各实施例技术方案的范围。Finally, it should be noted that: the above embodiments are only used to illustrate the technical solutions of the present invention, rather than limiting them; although the present invention has been described in detail with reference to the foregoing embodiments, those of ordinary skill in the art should understand that: It is still possible to modify the technical solutions described in the foregoing embodiments, or perform equivalent replacements for some or all of the technical features; and these modifications or replacements do not make the essence of the corresponding technical solutions deviate from the technical solutions of the various embodiments of the present invention. scope.

Claims (8)

1. An apparatus for preparing a liquid metal catalyst by plasma, comprising: the reaction chamber (9) and the sealing cover (8), wherein the reaction chamber (9) and the sealing cover (8) form a containing cavity; an aeration head (6), an aeration pipe (4), a first electrode (1) and a target metal salt solution (11) are arranged in the accommodating cavity, an insulating sleeve (5) is arranged in the aeration pipe (4), and a second electrode (10) is arranged in the insulating sleeve (5); the electrodes are respectively connected with a power high-voltage end and a grounding end, and when the first electrode (1) is grounded, the first electrode (1) outside the aerator pipe (4) can be omitted by utilizing the target metal salt solution (11) to be directly grounded;
one end of the aeration pipe (4) is provided with an aeration head (6), the other end of the aeration pipe is provided with a sealing plug (2), and the second electrode (10) is fixed in the aeration pipe (4) through the sealing plug (2).
2. An apparatus for preparing a liquid metal catalyst by means of plasma according to claim 1, characterized in that the aeration tube (4) is provided with a gas-guiding opening (3).
3. The apparatus for preparing a liquid metal catalyst by using plasma according to claim 2, wherein the aeration pipe (4) is provided with a plurality of micropores, and the inner diameter of the micropores is 0.2-2 mm.
4. An apparatus for preparing a liquid metal catalyst by means of plasma according to claim 1, characterized in that one end of the first electrode (1) is provided with a fastener (7), and the first electrode (1) is fixed with the sealing cover (8) by means of the fastener (7) and placed in the target metal salt solution (11).
5. An apparatus for preparing a liquid metal catalyst according to claim 1, characterized in that the first electrode (1) and the second electrode (10) are made of stainless steel or other electrically conductive material.
6. The apparatus for preparing a liquid metal catalyst by using plasma according to claim 1, wherein the power source is one of a pulse, a direct current and an alternating current power source.
7. A method for preparing a liquid metal catalyst based on the apparatus for preparing a liquid metal catalyst by plasma according to any one of claims 1 to 6, comprising the steps of:
step 1: preparing a target metal salt solution (11), adjusting the pH value to 7-10, and placing the prepared target metal salt solution into a reaction chamber (9);
step 2: and introducing carrier gas into the aeration pipe (4) and sealing the device, applying voltage to the first electrode (1) and the second electrode (10) to form plasma, and gradually generating the target metal catalyst in the solution by controlling one or more of discharge voltage, frequency and pulse width parameters.
8. The method for preparing a liquid metal catalyst by using a plasma apparatus for preparing a liquid metal catalyst according to claim 7, wherein the concentration of the target metal salt solution (11) in the step 1 is 0.1 to 1mol/L.
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