CN102390805A - Hydrogen production composition and preparation method thereof, and method for preparing hydrogen - Google Patents
Hydrogen production composition and preparation method thereof, and method for preparing hydrogen Download PDFInfo
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Abstract
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技术领域 technical field
本发明涉及氢能技术领域,主要涉及一种利用金属粉体的组合物进行自发水解制取氢气的方法。 The invention relates to the technical field of hydrogen energy, and mainly relates to a method for producing hydrogen by spontaneous hydrolysis of a metal powder composition.
背景技术 Background technique
氢气是一种非常有前途的可再生清洁能源,相比起其它的能源,氢能具有非常明显的优越性,因为氢的能量密度大,单位质量氢反应所释放的热能是汽油的三倍。而且,氢与氧反应唯一的产物就是水,不会对环境造成负面影响。特别是以氢气为原料的燃料电池和氢气发动机的问世,使世界范围内的汽车工业面临一场深刻的革命。要实现氢能的广泛运用,首先必须解决两个问题:1、氢气的现场供应;2、氢气的存储运输。目前常用的制氢方法有电解水制氢、化石能源制氢、生物制氢、烃类分解制氢、氨裂解制氢、硫化氢分解制氢、太阳能直接光电制氢、辐射性催化剂制氢、电子共振裂解水、氢化物水解制氢等等。而主要的储氢方法有高压气态储氢、液化储氢、金属氧化物储氢、碳质吸附储氢和化学氢化物储氢。 Hydrogen is a very promising renewable clean energy. Compared with other energy sources, hydrogen energy has a very obvious advantage, because hydrogen has a high energy density, and the heat energy released by hydrogen per unit mass is three times that of gasoline. Moreover, the only product of the hydrogen-oxygen reaction is water, which does not negatively impact the environment. In particular, the advent of fuel cells and hydrogen engines that use hydrogen as a raw material has brought about a profound revolution in the automotive industry worldwide. To realize the widespread use of hydrogen energy, two problems must first be solved: 1. On-site supply of hydrogen; 2. Storage and transportation of hydrogen. At present, the commonly used hydrogen production methods include electrolysis of water to produce hydrogen, fossil energy to produce hydrogen, biological hydrogen to produce hydrogen, hydrocarbon decomposition to produce hydrogen, ammonia cracking to produce hydrogen, hydrogen sulfide to decompose hydrogen to produce hydrogen, solar direct photoelectric hydrogen to produce hydrogen, radiation catalyst to produce hydrogen, Electron resonance cracking water, hydride hydrolysis hydrogen production and so on. The main hydrogen storage methods include high-pressure gaseous hydrogen storage, liquefied hydrogen storage, metal oxide hydrogen storage, carbonaceous adsorption hydrogen storage and chemical hydride hydrogen storage.
氢是质子交换膜燃料电池的高效燃料,但是,氢的生产、运输和储存在产业结构上还存在很大问题,特别对于便携式燃料电池的应用,现场制氢和供氢系统的建立非常迫切。金属氢化物储氢技术是一种可小型化的储氢技术方法,这种储氢方法尽管具有充放氢可逆性好、循环寿命长等优点,但是,由于金属的密度大,储氢容量低、储氢合金容易粉化,绝大多数金属的储氢质量分数为1.5 %~3 %,无法满足实用化要求。而在现有的化学品产氢技术中,氢化镁是其中一种产氢材料,它遇水可以发生水解,反应速率快,具有十分优良的放氢动力学性质。但氢化镁水解反应非常激烈,产氢速率难以控制,遇空气可自发燃烧,具有一定危险性,不利于保存,而且,氢化镁的价格昂贵,制氢成本高。 Hydrogen is an efficient fuel for proton exchange membrane fuel cells. However, there are still big problems in the industrial structure of hydrogen production, transportation and storage. Especially for the application of portable fuel cells, the establishment of on-site hydrogen production and hydrogen supply systems is very urgent. Metal hydride hydrogen storage technology is a miniaturized hydrogen storage technology method. Although this hydrogen storage method has the advantages of good reversibility of hydrogen charging and discharging and long cycle life, due to the high density of metals, the hydrogen storage capacity is low. 1. Hydrogen storage alloys are easy to pulverize, and the hydrogen storage mass fraction of most metals is 1.5%~3%, which cannot meet the practical requirements. In the existing chemical hydrogen production technology, magnesium hydride is one of the hydrogen production materials. It can be hydrolyzed when it meets water, the reaction rate is fast, and it has very good hydrogen desorption kinetic properties. However, the hydrolysis reaction of magnesium hydride is very intense, the rate of hydrogen production is difficult to control, and it can spontaneously combust when exposed to air, which is dangerous and not conducive to storage. Moreover, magnesium hydride is expensive and the cost of hydrogen production is high.
硼氢化物是一类化学储氢材料,以硼氢化钠为例,它在二十世纪五十年代开始用作还原剂时,人们就认识到它能水解产氢的特性,并加以利用。硼氢化钠作为一种良好的储氢材料能够在一定条件下稳定保存,它的半衰期长,在加碱情况下能稳定存在。目前利用硼氢化物水解制氢的方法主要是利用催化剂分解。为了改善产氢效果,一般都会将催化剂负载到高比表面积的基底上,但这种方法还是有很大的局限性:1,将催化剂负载到基底上的工艺过程复杂,同时在制作过程中会造成催化剂的损耗,增加催化剂的制作时间和成本;2,催化剂在基底上的附着力差,因为反应过程中产生的氢气会不断冲击基底上的催化剂,使催化剂从基底上脱落,影响反应的效果;3,硼氢化物溶液需要首先用强碱稳定,不仅实际应用困难,而且容易引起爬碱、粘接、腐蚀等问题;4,硼氢化物在反应过程中会不断地生成偏硼酸盐,对于高浓度的硼氢化物溶液,随着水解反应过程中水的不断消耗,偏硼酸盐会以胶体的形式存在于溶液中,这些胶体会覆盖在基底表面,抑制催化剂的催化效果,使反应速率很快衰减,从而难以实现大规模的稳定产氢[E.Y. Marrero-Alfonso, et al., Int. J. Hydrogen Energy, 2007, 32,4723-4730]。 Borohydride is a class of chemical hydrogen storage materials. Taking sodium borohydride as an example, when it was used as a reducing agent in the 1950s, people recognized its ability to produce hydrogen by hydrolysis and utilized it. As a good hydrogen storage material, sodium borohydride can be stored stably under certain conditions. It has a long half-life and can exist stably when alkali is added. At present, the method of hydrogen production by hydrolysis of borohydride mainly utilizes catalyst decomposition. In order to improve the hydrogen production effect, the catalyst is usually loaded on the substrate with high specific surface area, but this method still has great limitations: 1. The process of loading the catalyst on the substrate is complicated, and at the same time, it will 2. The adhesion of the catalyst on the substrate is poor, because the hydrogen generated during the reaction will continuously impact the catalyst on the substrate, causing the catalyst to fall off from the substrate and affect the effect of the reaction ; 3. The borohydride solution needs to be stabilized with a strong base first, which is not only difficult in practical application, but also easily causes problems such as alkali climbing, adhesion, and corrosion; 4. The borohydride will continuously generate metaborate during the reaction process. For high-concentration borohydride solutions, with the continuous consumption of water during the hydrolysis reaction, metaborate will exist in the solution in the form of colloids. These colloids will cover the surface of the substrate, inhibit the catalytic effect of the catalyst, and make the reaction The rate decays quickly, making it difficult to achieve large-scale stable hydrogen production [E.Y. Marrero-Alfonso, et al., Int. J. Hydrogen Energy, 2007, 32, 4723-4730].
中国专利[公开号CN 101568487A]披露了一种产氢组合物,其中涉及铝粉(氧化铝粉)、氧化钙、氢氧化钠、氯化物等组分。这种组合物能快速产氢,但是产氢速度较难调控。由于添加强碱组分用于溶解氢氧化铝,溶液的pH值较高;由于添加了氧化钙,反应体系发热严重,因为氧化钙溶解释放大量的热量,等等,造成使用不方便。 中国专利申请[申请号200810010747.X,200810229173.5]披露了一种解水铝制氢配方,用卤素化铝等与铝粉混合而成。这种配方需要一定的温度启动,因此需要辅助加热装置,便携式使用由有难度。 Chinese patent [publication number CN 101568487A] discloses a hydrogen production composition, which involves aluminum powder (alumina powder), calcium oxide, sodium hydroxide, chloride and other components. This composition can produce hydrogen quickly, but the rate of hydrogen production is difficult to control. Due to the addition of strong alkali components for dissolving aluminum hydroxide, the pH value of the solution is relatively high; due to the addition of calcium oxide, the reaction system generates serious heat, because the dissolution of calcium oxide releases a large amount of heat, etc., resulting in inconvenient use. Chinese patent application [Application No. 200810010747.X, 200810229173.5] discloses a formula for producing hydrogen by dehydrating aluminum, which is made by mixing aluminum halide and aluminum powder. This recipe needs a certain temperature to start, so it needs an auxiliary heating device, which makes it difficult to use portablely. the
发明内容 Contents of the invention
本发明的目的是在于克服现有金属粉体产氢技术上的不足,提供一种产氢组合物及其制备方法与制氢方法,本发明能实现方便、可控和稳定性高的现场供氢。 The purpose of the present invention is to overcome the deficiencies in the existing metal powder hydrogen production technology, and provide a hydrogen production composition and its preparation method and hydrogen production method. The present invention can realize convenient, controllable and highly stable on-site supply hydrogen.
本发明的目的通过以下技术方案实现: The object of the present invention is achieved through the following technical solutions:
一种产氢组合物,由金属粉体、活化剂和添加剂混合得到,所述的金属粉体为铝粉、镁粉或锌粉中的一种或两种以上的混合物;所述活化剂为氯化钠、氯化钾或氟化钠中的一种或两种以上的混合物;所述的添加剂为氢氧化钙、氢氧化钡或氯化钙中的一种或一种以上的混合物。 A hydrogen production composition obtained by mixing a metal powder, an activator and an additive, the metal powder being one or a mixture of two or more of aluminum powder, magnesium powder or zinc powder; the activator is One or more mixtures of sodium chloride, potassium chloride or sodium fluoride; the additive is one or more mixtures of calcium hydroxide, barium hydroxide or calcium chloride.
作为上述产氢组合物进一步优化的技术方案,所述金属粉体占组合物的重量比为50-90%;所述活化剂占组合物的重量比为0.1-20%;所述添加剂占组合物的重量比为0.1-30%。 As a technical solution for further optimization of the above-mentioned hydrogen production composition, the metal powder accounts for 50-90% by weight of the composition; the activator accounts for 0.1-20% by weight of the composition; The weight ratio of the substance is 0.1-30%.
作为上述产氢组合物进一步优化的技术方案,将所述金属粉体、活化剂和添加剂通过球磨混合均匀得所述产氢组合物。 As a technical solution for further optimization of the above-mentioned hydrogen-generating composition, the metal powder, activator and additive are uniformly mixed by ball milling to obtain the hydrogen-generating composition.
上述产氢组合物的制氢方法,将所述产氢组合物加入水中,即能稳定地产生氢气。 In the hydrogen production method of the above hydrogen production composition, adding the hydrogen production composition into water can stably generate hydrogen.
作为上述产氢组合物的制氢方法进一步优化的技术方案,其可通过改变产氢组合物的组成比例和/或改变产氢组合物与水的比例,控制产氢量、产氢速度和/或产氢时间。 As a technical solution for further optimizing the hydrogen production method of the above-mentioned hydrogen-producing composition, it can control the amount of hydrogen produced, the rate of hydrogen production and/or by changing the composition ratio of the hydrogen-producing composition and/or changing the ratio of the hydrogen-producing composition to water or hydrogen production time.
作为上述产氢组合物的制氢方法进一步优化的技术方案,所述金属粉体占组合物的重量比为50-99%。 As a technical solution for further optimizing the hydrogen production method of the above hydrogen production composition, the weight ratio of the metal powder to the composition is 50-99%.
作为上述产氢组合物的制氢方法进一步优化的技术方案,所述活化剂占组合物的重量比为0.5-20%。 As a technical solution for further optimizing the hydrogen production method of the above hydrogen production composition, the activator accounts for 0.5-20% by weight of the composition.
作为上述产氢组合物的制氢方法进一步优化的技术方案,所述添加剂占组合物的重量比为0.5-30%。 As a technical solution for further optimizing the hydrogen production method of the above hydrogen production composition, the weight ratio of the additive to the composition is 0.5-30%.
作为上述产氢组合物的制氢方法进一步优化的技术方案,所述的产氢组合物与水的重量比为1:200– 1:10。 As a technical solution for further optimizing the hydrogen production method of the above-mentioned hydrogen-producing composition, the weight ratio of the hydrogen-producing composition to water is 1:200-1:10.
与现有技术相比,本发明具有以下优点:1)采取活化金属表面的措施不同。铝等金属在水溶液中具有自分解产氢能力,但是由于产物如氢氧化铝形成表面膜,阻碍反应的进一步进行,所以单纯铝在水里的产氢速度非常慢。上述几个发明的原理是利用碱(如氢氧化钠)溶解氢氧化铝,因为氢氧化铝是两性化合物。但是加碱的结果使得溶液的pH值比较高。特别在质子交换膜燃料电池中使用,需要除去碱性成分,使用不方便。本发明的出发点是在组合物中添加能腐蚀破坏氢氧化铝膜的成分,使铝不断处于活化状态。而这种成分比碱更安全、更便宜、无毒无害。2)可以有效控制温度。利用碱性配方产氢反应体系的发热非常严重,提高温度则能提高反应速度,但在使用时存在安全隐患。本发明可方便地通过改变添加剂和水量来控制温度。3)通过选择适当组分比例,可以有效地控制产氢速率和时间。4)本发明的产氢组合物在空气中不吸潮,可以用无纺布等包装成袋,使用和保管都非常方便。5)可以实现现场供氢和持久供氢。本发明的优点还在于,使用产氢组合物制氢所用的制氢装置简单,对水的要求不高,可以重复使用。水溶液不需要像使用硼氢化钠那样加碱才能稳定,更换溶液容易。而且在大规模制氢应用时,产物容易回收,从而更节约成本。 Compared with the prior art, the present invention has the following advantages: 1) The measures for activating the metal surface are different. Metals such as aluminum have the ability to self-decompose to produce hydrogen in aqueous solution, but because the product such as aluminum hydroxide forms a surface film, which hinders the further progress of the reaction, the hydrogen production rate of pure aluminum in water is very slow. The principle of the above-mentioned several inventions is to utilize alkali (such as sodium hydroxide) to dissolve aluminum hydroxide, because aluminum hydroxide is an amphoteric compound. However, the addition of alkali results in a higher pH of the solution. Especially when used in proton exchange membrane fuel cells, alkaline components need to be removed, which is inconvenient to use. The starting point of the invention is to add components capable of corroding and destroying the aluminum hydroxide film in the composition, so that the aluminum is constantly in an activated state. And this ingredient is safer, cheaper, non-toxic and harmless than alkali. 2) The temperature can be effectively controlled. The heating of the hydrogen production reaction system using the alkaline formula is very serious, and increasing the temperature can increase the reaction speed, but there are safety hazards in use. The invention can conveniently control the temperature by changing the amount of additives and water. 3) The rate and time of hydrogen production can be effectively controlled by selecting an appropriate proportion of components. 4) The hydrogen production composition of the present invention does not absorb moisture in the air, and can be packed into bags with non-woven fabrics, etc., which are very convenient to use and store. 5) On-site hydrogen supply and long-term hydrogen supply can be realized. The invention also has the advantages that the hydrogen production device used for hydrogen production by using the hydrogen production composition is simple, has low requirements on water, and can be reused. The aqueous solution does not need to add alkali to be stable like sodium borohydride, and it is easy to replace the solution. Moreover, in the application of large-scale hydrogen production, the product is easy to recover, thereby saving costs.
具体实施方式 Detailed ways
实施例1 Example 1
将占原料质量分数为99%的铝粉与0.5%氯化钠及0.5%氢氧化钙混合,球磨1小时,得产氢组合物。 The aluminum powder accounting for 99% of the raw material mass fraction was mixed with 0.5% sodium chloride and 0.5% calcium hydroxide, and ball milled for 1 hour to obtain a hydrogen-producing composition. the
实施例2 Example 2
将占原料质量分数50%的铝粉与20%的氯化钠及30%的氢氧化钙混合,球磨1小时,得产氢组合物。用无纺布包装成袋,浸在10倍产氢组合物质量的水中,可以5升/分的速度连续产氢。 Mix aluminum powder accounting for 50% of the mass fraction of raw materials with 20% sodium chloride and 30% calcium hydroxide, and ball mill for 1 hour to obtain a hydrogen-producing composition. It is packaged into a bag with non-woven fabric, soaked in water 10 times the mass of the hydrogen production composition, and can continuously produce hydrogen at a speed of 5 liters per minute.
实施例3 Example 3
将占原料质量分数为90%的铝粉与9.9%氯化钠及0.1%氢氧化钙混合,球磨1小时,得产氢组合物。用无纺布包装成袋,浸在200倍产氢组合物质量的水中,可以0.5升/分的速度连续产氢。 Mix 90% aluminum powder with 9.9% sodium chloride and 0.1% calcium hydroxide, and ball mill for 1 hour to obtain a hydrogen-producing composition. It is packaged into a bag with non-woven fabric, soaked in water 200 times the mass of the hydrogen production composition, and can continuously produce hydrogen at a rate of 0.5 liters per minute.
实施例4 Example 4
将占原料质量分数为90%的铝粉与0.1%氯化钠、6%氯化钙及3.9%氢氧化钙混合,球磨1小时,得产氢组合物。用无纺布包装成袋,浸在50倍产氢组合物质量的水中,可以1升/分的速度连续产氢。 The aluminum powder accounting for 90% of the raw material mass fraction was mixed with 0.1% sodium chloride, 6% calcium chloride and 3.9% calcium hydroxide, and ball milled for 1 hour to obtain a hydrogen-producing composition. It is packaged into a bag with non-woven fabric, soaked in water 50 times the mass of the hydrogen production composition, and can continuously produce hydrogen at a rate of 1 liter/min.
实施例5 Example 5
将质量为15克的铝粉与0.2克氯化钠、1克氯化钙及0.2克氢氧化钙混合,球磨1小时,得产氢组合物。用无纺布包装成袋,浸在300毫升水中可以50毫升/分的速度连续产氢4小时以上。 Mix 15 g of aluminum powder with 0.2 g of sodium chloride, 1 g of calcium chloride and 0.2 g of calcium hydroxide, and ball mill for 1 hour to obtain a hydrogen-producing composition. It is packaged into a bag with non-woven fabric, soaked in 300 ml of water, and can continuously produce hydrogen at a rate of 50 ml/min for more than 4 hours.
实施例6 Example 6
将质量为30克的铝粉与2克氯化钠、1.5克氯化钙混合,球磨1小时,得产氢组合物。用无纺布包装成袋,浸在500毫升水中可以600毫升/分的速度连续产氢1小时。 Mix 30 grams of aluminum powder with 2 grams of sodium chloride and 1.5 grams of calcium chloride, and ball mill for 1 hour to obtain a hydrogen-producing composition. It is packaged into a bag with non-woven fabric, soaked in 500 ml of water, and can continuously produce hydrogen at a rate of 600 ml/min for 1 hour.
实施例7 Example 7
将实施例1-4中的氢氧化钙换成氢氧化钡,球磨1小时,得产氢组合物。 The calcium hydroxide in Examples 1-4 was replaced by barium hydroxide, and ball milled for 1 hour to obtain a hydrogen-producing composition.
实施例8 Example 8
将实施例1-4中的氯化钠换成氯化钾,球磨1小时,得产氢组合物。 The sodium chloride in Example 1-4 was replaced with potassium chloride, and ball milled for 1 hour to obtain a hydrogen-producing composition.
实施例9 Example 9
将实施例1-4中的氯化钠换成氟化钠,球磨1小时,得产氢组合物。 The sodium chloride in Examples 1-4 was replaced with sodium fluoride, and ball milled for 1 hour to obtain a hydrogen-producing composition. the
实施例10 Example 10
将实施例1-4、7-9中的铝换成镁,球磨1小时,得产氢组合物。 The aluminum in Examples 1-4 and 7-9 was replaced by magnesium, and ball milled for 1 hour to obtain a hydrogen-producing composition.
实施例11 Example 11
将实施例1-4、7-9中的铝换成锌,球磨1小时,得产氢组合物。 The aluminum in Examples 1-4 and 7-9 was replaced with zinc, and ball milled for 1 hour to obtain a hydrogen-producing composition.
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| CN103342340A (en) * | 2013-07-10 | 2013-10-09 | 北京依米康科技发展有限公司 | Fast hydrogen producing agent |
| CN103787273A (en) * | 2014-01-21 | 2014-05-14 | 四川大学 | Magnesium-calcium-based hydride powder for wide-temperature zone hydrolysis hydrogen generation and preparation method for magnesium-calcium-based hydride powder |
| CN105819399A (en) * | 2016-03-28 | 2016-08-03 | 浙江吉利控股集团有限公司 | Hydrogen production reaction with controllable hydrogen production speed |
| CN106044707A (en) * | 2016-06-01 | 2016-10-26 | 江门市绿茵环保科技有限公司 | Mixture reacted with water vapor to prepare hydrogen and preparation method and application method thereof |
| TWI570059B (en) * | 2014-10-22 | 2017-02-11 | Get Green Energy Corp Ltd | Hydrogen production composition and hydrogen production method |
| CN107174975A (en) * | 2017-06-18 | 2017-09-19 | 长沙无道工业设计有限公司 | A kind of desalinization composite membrane for producing hydrogen-rich direct drinking and preparation method thereof |
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| CN107459018A (en) * | 2017-07-12 | 2017-12-12 | 上海华普汽车有限公司 | Aluminum-base composite hydrogen production agent, preparation method and applications |
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| CN109824013A (en) * | 2019-03-27 | 2019-05-31 | 武汉市能智达科技有限公司 | Application, magnesium hydride hydrogen manufacturing mix reagent and the magnesium hydride hydrogen production process of magnesium hydride hydrogen manufacturing auxiliary agent |
| CN111481425A (en) * | 2019-01-25 | 2020-08-04 | 曹荣华 | Microenvironment hydrogen supply breathable layer and external application bag |
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| CN103342340B (en) * | 2013-07-10 | 2014-08-20 | 北京依米康科技发展有限公司 | Fast hydrogen producing agent |
| CN103342340A (en) * | 2013-07-10 | 2013-10-09 | 北京依米康科技发展有限公司 | Fast hydrogen producing agent |
| CN103787273A (en) * | 2014-01-21 | 2014-05-14 | 四川大学 | Magnesium-calcium-based hydride powder for wide-temperature zone hydrolysis hydrogen generation and preparation method for magnesium-calcium-based hydride powder |
| CN103787273B (en) * | 2014-01-21 | 2015-12-30 | 四川大学 | For the magnesium calcium base hydride powder and preparation method thereof of wide warm area hydrolytic hydrogen production |
| TWI570059B (en) * | 2014-10-22 | 2017-02-11 | Get Green Energy Corp Ltd | Hydrogen production composition and hydrogen production method |
| CN105819399A (en) * | 2016-03-28 | 2016-08-03 | 浙江吉利控股集团有限公司 | Hydrogen production reaction with controllable hydrogen production speed |
| CN106044707B (en) * | 2016-06-01 | 2018-12-25 | 江门市绿茵环保科技有限公司 | The mixture and preparation method, application method of hydrogen are prepared with steam reaction |
| CN106044707A (en) * | 2016-06-01 | 2016-10-26 | 江门市绿茵环保科技有限公司 | Mixture reacted with water vapor to prepare hydrogen and preparation method and application method thereof |
| CN107174975A (en) * | 2017-06-18 | 2017-09-19 | 长沙无道工业设计有限公司 | A kind of desalinization composite membrane for producing hydrogen-rich direct drinking and preparation method thereof |
| CN107174975B (en) * | 2017-06-18 | 2020-06-09 | 玛雅森林(北京)国际科技有限公司 | Seawater desalination composite membrane for producing hydrogen-rich direct drinking water and preparation method thereof |
| CN107434986A (en) * | 2017-06-28 | 2017-12-05 | 广西启明氢能源有限公司 | Hydrous ethanol reforms fuel combination dedicated liquid activator |
| CN107459018B (en) * | 2017-07-12 | 2020-04-21 | 上海华普汽车有限公司 | Aluminum-based composite hydrogen-producing agent, preparation method and application thereof |
| CN107459018A (en) * | 2017-07-12 | 2017-12-12 | 上海华普汽车有限公司 | Aluminum-base composite hydrogen production agent, preparation method and applications |
| CN109592637A (en) * | 2018-12-29 | 2019-04-09 | 杭州氢源素生物科技有限公司 | A kind of magnesium powder hydrogen manufacturing stick and preparation method thereof |
| CN111481425A (en) * | 2019-01-25 | 2020-08-04 | 曹荣华 | Microenvironment hydrogen supply breathable layer and external application bag |
| CN109824013A (en) * | 2019-03-27 | 2019-05-31 | 武汉市能智达科技有限公司 | Application, magnesium hydride hydrogen manufacturing mix reagent and the magnesium hydride hydrogen production process of magnesium hydride hydrogen manufacturing auxiliary agent |
| CN115872357A (en) * | 2023-02-24 | 2023-03-31 | 四川卡文智氢新能源有限公司 | Modified aluminum hydrolysis hydrogen production material and preparation method and application thereof |
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