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CN107549299A - A kind of Ethyl formate administration system fumigated for fruit and method - Google Patents

A kind of Ethyl formate administration system fumigated for fruit and method Download PDF

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CN107549299A
CN107549299A CN201710873109.XA CN201710873109A CN107549299A CN 107549299 A CN107549299 A CN 107549299A CN 201710873109 A CN201710873109 A CN 201710873109A CN 107549299 A CN107549299 A CN 107549299A
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ethyl formate
nitrogen
gas
tank body
fumigated
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刘涛
李丽
张广平
李柏树
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Chinese Academy of Inspection and Quarantine CAIQ
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Chinese Academy of Inspection and Quarantine CAIQ
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Abstract

本发明提供一种用于水果熏蒸的甲酸乙酯投药系统及方法,该系统包括氮气供应单元、甲酸乙酯气化单元及甲酸乙酯稀释混合释放单元;氮气供应单元含氮气源及氮气出口;甲酸乙酯气化单元含具不锈钢内壁的罐体,设有液体甲酸乙酯进口、氮气进口、甲酸乙酯气体出口及加热模块;甲酸乙酯稀释混合释放单元包括具有防爆设计的不锈钢罐体,设有甲酸乙酯气体进口、循环空气进口及混合气体出口,该循环空气进口及该混合气体出口分别通过管路与盛放待熏蒸物容器的熏蒸空间连通,以将该稀释混合后的混合气体输入到该熏蒸空间,及将该熏蒸空间的空气循环输入该不锈钢罐体内。该系统具有可直接使用液态的甲酸乙酯、气化迅速、使用经济及操作安全等优势。

The invention provides an ethyl formate dosing system and method for fruit fumigation. The system includes a nitrogen supply unit, an ethyl formate gasification unit, and an ethyl formate dilution mixing release unit; the nitrogen supply unit contains a nitrogen source and a nitrogen outlet; The ethyl formate gasification unit includes a tank with a stainless steel inner wall, which is equipped with a liquid ethyl formate inlet, a nitrogen gas inlet, an ethyl formate gas outlet and a heating module; the ethyl formate dilution mixing release unit includes a stainless steel tank with an explosion-proof design, Equipped with an ethyl formate gas inlet, a circulating air inlet and a mixed gas outlet, the circulating air inlet and the mixed gas outlet are respectively communicated with the fumigation space of the container to be fumigated through pipelines, so that the diluted mixed gas input into the fumigation space, and the air circulation of the fumigation space is input into the stainless steel tank. The system has the advantages of direct use of liquid ethyl formate, rapid gasification, economical use and safe operation.

Description

一种用于水果熏蒸的甲酸乙酯投药系统及方法Ethyl formate dosing system and method for fruit fumigation

技术领域technical field

本发明涉及一种用于水果熏蒸的投药系统及方法,尤其涉及一种用于水果熏蒸的甲酸乙酯投药系统及方法,属于检疫领域。The invention relates to a dosing system and method for fruit fumigation, in particular to an ethyl formate dosing system and method for fruit fumigation, belonging to the field of quarantine.

背景技术Background technique

全球经济一体化、国际贸易形式多样化和世界政治经济格局的重新改变,导致外来有害生物入侵频率加大,严重威胁我国生态环境、农业生产和粮食安全。检疫处理是世界各国通用的外来有害生物防控的主要技术手段和官方行为。根据WTO相关协议,出口国有义务保证出口产品不携带进口国关注的有害生物。因而,是否具有有效的检疫处理措施,经常成为农产品国际市场准入谈判的焦点,也被作为技术性贸易措施广泛应用。Global economic integration, diversification of international trade forms, and changes in the world's political and economic structure have led to an increase in the frequency of alien pest invasions, seriously threatening my country's ecological environment, agricultural production, and food security. Quarantine treatment is the main technical means and official action for the prevention and control of alien pests commonly used in countries all over the world. According to relevant WTO agreements, exporting countries are obliged to ensure that exported products do not carry harmful organisms of concern to importing countries. Therefore, whether there are effective quarantine treatment measures often becomes the focus of negotiations on international market access for agricultural products, and is also widely used as technical trade measures.

新鲜水果是最易携带有害生物的货物,检疫风险极高。对于水果的检疫处理,目前以溴甲烷熏蒸为主。自上世纪五六十年代以来,欧美等发达国家建立了以溴甲烷熏蒸为核心的检疫处理技术和标准体系。我国也在八十年代后快速跟进,结合中国进出境贸易特点,建立了具有我国特色的以溴甲烷熏蒸为基础的技术体系。本世纪以来,环境保护和气候变化给检疫处理提出了新的技术需求。溴甲烷作为“蒙特利尔议定书”管控的臭氧层耗减物质必须逐渐淘汰。国际社会针对溴甲烷替代物开展了大量研究,结果表明甲酸乙酯是比较有前途的新型水果熏蒸剂。Fresh fruit is the cargo most likely to carry pests, and the risk of quarantine is extremely high. For the quarantine treatment of fruits, methyl bromide fumigation is currently the main method. Since the 1950s and 1960s, developed countries such as Europe and the United States have established quarantine treatment technology and standard systems centered on methyl bromide fumigation. my country also followed up quickly after the 1980s, and combined with the characteristics of China's inbound and outbound trade, established a technical system based on methyl bromide fumigation with Chinese characteristics. Since the beginning of this century, environmental protection and climate change have put forward new technical requirements for quarantine treatment. As an ozone depleting substance controlled by the Montreal Protocol, methyl bromide must be phased out. The international community has carried out a lot of research on methyl bromide substitutes, and the results show that ethyl formate is a promising new fruit fumigant.

甲酸乙酯是一种天然存在物质,在水果中一般含有约5~10ppm的甲酸乙酯,同时甲酸乙酯易自然分解为甲酸和乙醇,因而使用甲酸乙酯一般不存在残留和食品安全问题。事实上,甲酸乙酯被用做食品添加剂已有近70年历史,美国FDA也把甲酸乙酯认定为“一般认为是安全的物质”(GRAS),不需规定残留限量标准。近年来的研究表明,甲酸乙酯虽然对水果的穿透能力较差,不能杀灭实蝇等水果内部的害虫,但对水果表面的有害生物如粉蚧等有很好的杀灭效果。一般甲酸乙酯用于熏蒸的剂量为40~80g/m3,熏蒸时间为3~6h。Ethyl formate is a naturally occurring substance. Fruits generally contain about 5-10ppm of ethyl formate. At the same time, ethyl formate is easily decomposed into formic acid and ethanol naturally. Therefore, there are generally no residues and food safety problems when using ethyl formate. In fact, ethyl formate has been used as a food additive for nearly 70 years, and the U.S. FDA has also identified ethyl formate as a "generally recognized as safe substance" (GRAS), and there is no need to specify residue limits. Studies in recent years have shown that although ethyl formate has poor penetrating ability to fruits and cannot kill pests inside fruits such as fruit flies, it has a good killing effect on harmful organisms on the surface of fruits such as mealybugs. Generally, the dose of ethyl formate used for fumigation is 40~80g/m 3 , and the fumigation time is 3~6h.

但是,使用甲酸乙酯进行熏蒸面临一些应用方面的问题,主要是:However, fumigation with ethyl formate faces some application problems, mainly:

(1)甲酸乙酯的沸点一般为53.4~54.4℃,因而在常温常压下是液态,必须气化后才能进行熏蒸,同时考虑到甲酸乙酯的熏蒸时间一般较短(3~6h),所以要求气化应在较快速度下进行,一般气化和投药时间需控制在20min以内;(1) The boiling point of ethyl formate is generally 53.4-54.4°C, so it is liquid at normal temperature and pressure, and must be vaporized before fumigation. Considering that the fumigation time of ethyl formate is generally short (3-6h), Therefore, it is required that the gasification should be carried out at a relatively fast speed, and the general gasification and dosing time should be controlled within 20 minutes;

(2)甲酸乙酯易燃易爆,甲酸乙酯气体在空气中的爆炸下限为2.7%(v/v),约合90g/m3(2) Ethyl formate is flammable and explosive. The lower explosion limit of ethyl formate gas in air is 2.7% (v/v), which is about 90g/m 3 .

为了安全有效的使用甲酸乙酯熏蒸,有研究者提出将CO2和甲酸乙酯(质量比6:1)混装在高压钢瓶中,使用CO2和甲酸乙酯混合气体进行熏蒸。这样在使用过程中也有一定问题:In order to use ethyl formate safely and effectively for fumigation, some researchers proposed to mix CO2 and ethyl formate (mass ratio 6:1) in a high-pressure steel cylinder, and use the mixed gas of CO2 and ethyl formate for fumigation. In this way, there are certain problems in the process of use:

(1)熏蒸一般在港口(海港或空港)进行,高压钢瓶的装运、储存和运输不方便;(1) Fumigation is generally carried out in ports (seaports or airports), and the shipment, storage and transportation of high-pressure steel cylinders are inconvenient;

(2)混合气体用量较大,消耗太快。以一般集装箱熏蒸为例,20英尺集装箱的体积约33m3,按投药量60g/m3计算,需约2kg甲酸乙酯,一个高压钢瓶可装载15~18kg混合气体,这样熏蒸一个20英尺集装箱就需要1个高压钢瓶,不够经济,且又增加了装运和储存成本。(2) The amount of mixed gas is large and consumed too quickly. Taking general container fumigation as an example, the volume of a 20-foot container is about 33m 3 , based on the dosage of 60g/m 3 , about 2kg of ethyl formate is needed, and a high-pressure steel cylinder can hold 15-18kg of mixed gas, so fumigation of a 20-foot container is One high-pressure steel cylinder is required, which is not economical and increases shipping and storage costs.

(3)投药速度较慢。由于甲酸乙酯和二氧化碳混合气体以液态形式储存于高压钢瓶中,主要是通过自身在钢瓶内部气化的压力驱动,释放出钢瓶,因此在投药初始阶段还能维持较快速度,但随着内部药剂量减少,同时在投药过程中消耗了大量热量用于气化,在投药后期,钢瓶温度下降,内部压力急剧衰减,投药速度极慢。(3) Dosing speed is slow. Since the mixed gas of ethyl formate and carbon dioxide is stored in a high-pressure cylinder in liquid form, it is mainly driven by the pressure of its own gasification inside the cylinder to release the cylinder, so it can maintain a relatively fast speed at the initial stage of dosing, but as the internal The dose of medicine is reduced, and a large amount of heat is consumed for gasification during the dosing process. In the later stage of dosing, the temperature of the steel cylinder drops, the internal pressure decays sharply, and the dosing speed is extremely slow.

(4)投药过程中局部浓度过高。以混合气体形式投药,甲酸乙酯在进入集装箱时的浓度约为280g/m3,远高于90g/m3的最低爆炸极限。当然,由于混合气体中存在大量二氧化碳,可以减轻部分爆炸风险,但还缺乏系统科学的实验数据的支撑。(4) The local concentration is too high during the administration process. Dosing in the form of mixed gas, the concentration of ethyl formate when entering the container is about 280g/m 3 , much higher than the lowest explosion limit of 90g/m 3 . Of course, due to the presence of a large amount of carbon dioxide in the mixed gas, part of the risk of explosion can be mitigated, but there is still a lack of support from systematic and scientific experimental data.

(5)价格较高。以商品化的CO2和甲酸乙酯混合剂型Vapormate为例,1个20L钢瓶的价格约为3000元人民币,考虑到一个钢瓶仅能熏蒸1个20英尺的集装箱(一般可装载约10吨水果),每吨水果仅处理的药剂费用就高达300元。(5) The price is higher. Taking the commercialized CO2 and ethyl formate mixed formulation Vapormate as an example, the price of a 20L steel cylinder is about 3,000 RMB, considering that a steel cylinder can only fumigate a 20-foot container (generally, it can hold about 10 tons of fruit) , The cost of chemicals per ton of fruit is as high as 300 yuan.

因此,为了克服上述问题,本领域亟需开发一种新的一种用于水果熏蒸的甲酸乙酯投药系统及方法。Therefore, in order to overcome the above problems, there is an urgent need in the art to develop a new ethyl formate dosing system and method for fruit fumigation.

发明内容Contents of the invention

为了解决甲酸乙酯熏蒸中存在的问题,更好的使用甲酸乙酯,本发明的主要目的在于开发一种用于水果熏蒸的甲酸乙酯投药方法,该方法使用投药系统,该系统及方法具有可直接使用液态的甲酸乙酯、气化迅速、使用经济及操作安全等优势。In order to solve the problems existing in ethyl formate fumigation, use ethyl formate better, the main purpose of the present invention is to develop a kind of ethyl formate dosing method that is used for fruit fumigation, this method uses dosing system, this system and method have It can directly use liquid ethyl formate, has the advantages of rapid gasification, economical use and safe operation.

本发明的再一目的在于提供可应用于前述投药方法的甲酸乙酯投药系统。Another object of the present invention is to provide an ethyl formate drug delivery system that can be applied to the aforementioned drug delivery methods.

为此,本发明提供一种用于水果熏蒸的甲酸乙酯投药方法,所述方法使用甲酸乙酯投药系统,该甲酸乙酯投药系统包括氮气供应单元、甲酸乙酯气化单元及甲酸乙酯稀释混合释放单元;For this reason, the present invention provides a kind of ethyl formate dosing method for fumigation of fruit, described method uses ethyl formate dosing system, and this ethyl formate dosing system comprises nitrogen supply unit, ethyl formate gasification unit and ethyl formate Dilution mixed release unit;

所述氮气供应单元包括氮气源及氮气出口;The nitrogen supply unit includes a nitrogen source and a nitrogen outlet;

所述甲酸乙酯气化单元包括具不锈钢内壁的罐体,在该罐体上设有液体甲酸乙酯进口、氮气进口及甲酸乙酯气体出口;所述氮气进口垂直朝向该罐体的底部,其通过管路与所述氮气出口相连,位于工作时甲酸乙酯液面上方;该罐体还设有用于加热液体甲酸乙酯的加热模块;Described ethyl formate gasification unit comprises the tank body of tool stainless steel inner wall, is provided with liquid ethyl formate inlet, nitrogen gas inlet and ethyl formate gas outlet on this tank body; Described nitrogen gas inlet is vertically towards the bottom of this tank body, It is connected to the nitrogen outlet through a pipeline, and is located above the ethyl formate liquid level during work; the tank body is also provided with a heating module for heating liquid ethyl formate;

所述甲酸乙酯稀释混合释放单元包括具有防爆设计的不锈钢罐体,在该罐体上设有甲酸乙酯气体进口、循环空气进口及混合气体出口;所述甲酸乙酯气体进口通过管路与所述甲酸乙酯气体出口相连;该循环空气进口及该混合气体出口分别通过管路与盛放待熏蒸物容器的熏蒸空间连通,以将该稀释混合后的混合气体输入到该熏蒸空间,及将该熏蒸空间的空气循环输入该不锈钢罐体内;该甲酸乙酯投药方法包括如下步骤:The ethyl formate dilution mixing releasing unit comprises the stainless steel tank body with explosion-proof design, is provided with ethyl formate gas inlet, circulating air inlet and mixed gas outlet on this tank body; Described ethyl formate gas inlet passes pipeline and The ethyl formate gas outlet is connected; the circulating air inlet and the mixed gas outlet are respectively communicated with the fumigation space containing the container to be fumigated through pipelines, so that the diluted mixed gas is input into the fumigation space, and The air circulation of the fumigation space is input in the stainless steel tank; the ethyl formate dosing method comprises the following steps:

开启所述氮气单元向整个所述甲酸乙酯投药系统内供应氮气;Open the nitrogen unit to supply nitrogen to the entire ethyl formate dosing system;

从所述液体甲酸乙酯进口向所述具不锈钢内壁的罐体内供应液体甲酸乙酯,通过所述加热模块加热液体甲酸乙酯使其气化,气化后的甲酸乙酯气体在氮气的携带下从所述甲酸乙酯气体出口进入所述甲酸乙酯稀释混合释放单元,然后与来自于盛放待熏蒸物容器的熏蒸空间的空气混合稀释,最后从所述混合气体出口进入熏蒸空间;Liquid ethyl formate is supplied from the liquid ethyl formate inlet to the tank with stainless steel inner wall, and the liquid ethyl formate is heated by the heating module to make it gasified, and the gasified ethyl formate gas is carried by nitrogen Next, enter the ethyl formate dilution mixing release unit from the ethyl formate gas outlet, then mix and dilute with the air from the fumigation space containing the container to be fumigated, and finally enter the fumigation space from the mixed gas outlet;

控制甲酸乙酯气体进口气量/循环空气进口气量=1/20,使得所述混合气体出口甲酸乙酯的浓度在60~80g/m3Control ethyl formate gas inlet gas volume/circulating air inlet gas volume=1/20, so that the concentration of ethyl formate at the outlet of the mixed gas is 60~80g/m 3 ;

供应氮气的流速控制在190~250L/min;The flow rate of nitrogen supply is controlled at 190-250L/min;

在所述氮气出口与所述氮气进口的连接管路上还设有用于加热氮气的气体加热器;供应的氮气经所述气体加热器加热,该气体加热器的功率为1~3Kw,被加热后的氮气温度130~150℃。A gas heater for heating nitrogen is also provided on the connecting pipeline between the nitrogen outlet and the nitrogen inlet; the supplied nitrogen is heated by the gas heater, and the power of the gas heater is 1-3Kw, after being heated The nitrogen temperature is 130-150°C.

本发明氮气进口之所以垂直朝向该罐体的底部并且对其进行加热主要是由于甲酸乙酯具有燃爆特性,且易在过热时分解为甲酸和乙醇,因而使用加热板对甲酸乙酯加热的功率不能过大,考虑到甲酸乙酯气化潜热较高,在气化罐体内仅靠加热板加热沸腾气化速率较低,液体底部和上部温度差异较大,为此增加了顶部吹扫,一方面可以提高整个罐体上部温度,加速气化;也可以对甲酸乙酯液体进行扰动,增加分子活动,平衡上下部甲酸乙酯液体温度;采用这种方式,可显著加快甲酸乙酯液体的气化速度和排除速度,使得气化和投药时间可控制在20min以内,而不采用这种方式,气化和投药时间延长至40min以上,导致投药时间过长,失去应用价值(一般水果熏蒸时间仅为2~4h)。The reason why the nitrogen inlet of the present invention is vertically towards the bottom of the tank body and is heated is mainly because ethyl formate has explosive characteristics, and is easy to be decomposed into formic acid and ethanol when overheated, thus using a heating plate to heat ethyl formate The power should not be too large. Considering the latent heat of vaporization of ethyl formate is high, the vaporization rate is low in the gasification tank only by heating and boiling on the heating plate, and the temperature difference between the bottom and the upper part of the liquid is large. Therefore, the top purge is added. On the one hand, it can increase the temperature of the upper part of the whole tank and accelerate the gasification; it can also disturb the ethyl formate liquid, increase the molecular activity, and balance the temperature of the upper and lower part of the ethyl formate liquid; in this way, the ethyl formate liquid can be significantly accelerated. Gasification speed and removal speed, so that the gasification and dosing time can be controlled within 20 minutes, without this method, the gasification and dosing time will be extended to more than 40 minutes, resulting in too long dosing time and loss of application value (general fruit fumigation time Only 2 ~ 4h).

作为上述甲酸乙酯投药方法的一具体实施方式,优选地,在所述循环空气进口或混合气体出口与所述熏蒸空间的连接管路上设有密闭风机,以加速混合气体的输出及循环空气的输入。As a specific implementation of the above-mentioned ethyl formate dosing method, preferably, an airtight fan is provided on the connecting pipeline between the circulating air inlet or the mixed gas outlet and the fumigation space, so as to accelerate the output of the mixed gas and the circulation of the circulating air. enter.

作为上述甲酸乙酯投药方法的一具体实施方式,优选地,所述加热模块为陶瓷发热元件加热模块;优选地,其设于所述具不锈钢内壁的罐体的底部,其配有过热终止加热设计;更优选地,该陶瓷发热元件加热模块与液体甲酸乙酯接触的换热面积不低于300cm2,加热功率为3~6Kw,极限加热温度不高于180℃。As a specific implementation of the above ethyl formate dosing method, preferably, the heating module is a ceramic heating element heating module; preferably, it is arranged at the bottom of the tank body with a stainless steel inner wall, and it is equipped with an overheating termination heating module. Design; more preferably, the heat exchange area of the ceramic heating element heating module in contact with liquid ethyl formate is not less than 300cm 2 , the heating power is 3-6Kw, and the limit heating temperature is not higher than 180°C.

作为上述甲酸乙酯投药方法的一具体实施方式,优选地,所述具不锈钢内壁的罐体还设有残渣排放口。As a specific implementation of the above ethyl formate dosing method, preferably, the tank body with a stainless steel inner wall is also provided with a residue discharge port.

作为上述甲酸乙酯投药方法的一具体实施方式,优选地,所述氮气进口还配有气体流量计;所述甲酸乙酯气体进口和所述循环空气进口分别配有气体流量计。As a specific implementation of the above ethyl formate dosing method, preferably, the nitrogen inlet is also equipped with a gas flow meter; the ethyl formate gas inlet and the circulating air inlet are respectively equipped with a gas flow meter.

另一方面,本发明提供一种用于水果熏蒸的甲酸乙酯投药系统,其中,该甲酸乙酯投药系统包括氮气供应单元、甲酸乙酯气化单元及甲酸乙酯稀释混合释放单元;In another aspect, the present invention provides an ethyl formate dosing system for fruit fumigation, wherein the ethyl formate dosing system includes a nitrogen supply unit, an ethyl formate gasification unit and an ethyl formate dilution mixing release unit;

所述氮气供应单元包括氮气源及氮气出口;The nitrogen supply unit includes a nitrogen source and a nitrogen outlet;

所述甲酸乙酯气化单元包括具不锈钢内壁的罐体,在该罐体上设有液体甲酸乙酯进口、氮气进口及甲酸乙酯气体出口;所述氮气进口垂直朝向该罐体的底部,其通过管路与所述氮气出口相连,位于工作时甲酸乙酯液面上方;该罐体还设有用于加热液体甲酸乙酯的加热模块;Described ethyl formate gasification unit comprises the tank body of tool stainless steel inner wall, is provided with liquid ethyl formate inlet, nitrogen gas inlet and ethyl formate gas outlet on this tank body; Described nitrogen gas inlet is vertically towards the bottom of this tank body, It is connected to the nitrogen outlet through a pipeline, and is located above the ethyl formate liquid level during work; the tank body is also provided with a heating module for heating liquid ethyl formate;

所述甲酸乙酯稀释混合释放单元包括具有防爆设计的不锈钢罐体,在该罐体上设有甲酸乙酯气体进口、循环空气进口及混合气体出口;所述甲酸乙酯气体进口通过管路与所述甲酸乙酯气体出口相连;该循环空气进口及该混合气体出口分别通过管路与盛放待熏蒸物容器(例如集装箱)的熏蒸空间连通(一般是分别与熏蒸空间的上部和下部连接),以将该稀释混合后的混合气体输入到该熏蒸空间,及将该熏蒸空间的空气循环输入该不锈钢罐体内;The ethyl formate dilution mixing releasing unit comprises the stainless steel tank body with explosion-proof design, is provided with ethyl formate gas inlet, circulating air inlet and mixed gas outlet on this tank body; Described ethyl formate gas inlet passes pipeline and The ethyl formate gas outlet is connected; the circulating air inlet and the mixed gas outlet are respectively communicated with the fumigation space of the container to be fumigated (such as a container) through pipelines (generally connected to the upper and lower parts of the fumigation space respectively) , so that the diluted mixed gas is input into the fumigation space, and the air in the fumigation space is circulated into the stainless steel tank;

在所述氮气出口与所述氮气进口的连接管路上还设有用于加热氮气的气体加热器。A gas heater for heating nitrogen is also provided on the connecting pipeline between the nitrogen outlet and the nitrogen inlet.

本发明所述氮气单元的主要作用在于向系统提供氮气(纯度一般不低于99.9%的工业氮气),以氮气为保护气及携带气,将气化后的甲酸乙酯气体携带进混合罐体(具有防爆设计的不锈钢罐体)。The main function of the nitrogen unit of the present invention is to provide nitrogen (industrial nitrogen with a purity of not less than 99.9%) to the system, and use nitrogen as the protective gas and carrying gas to carry the vaporized ethyl formate gas into the mixing tank (stainless steel tank with explosion-proof design).

本发明所述甲酸乙酯气化单元的主要作用在于使用加热元件加热甲酸乙酯至沸腾,使液态甲酸乙酯气化成甲酸乙酯气体。为了使氮气能携带甲酸乙酯气体,前述氮气进口需位于工作时液态甲酸乙酯(工作液面)的上方,及时带走经沸腾气化的甲酸乙酯气体,同时其需要垂直朝向罐体底部,即在工作时使加热的氮气流朝向液面,以帮助甲酸乙酯气化。The main function of the ethyl formate gasification unit of the present invention is to use a heating element to heat the ethyl formate to boiling, so that the liquid ethyl formate is vaporized into ethyl formate gas. In order for nitrogen to carry ethyl formate gas, the aforementioned nitrogen gas inlet needs to be located above the liquid ethyl formate (working liquid level) during operation, so as to take away the boiled and vaporized ethyl formate gas in time, and it needs to be vertical to the bottom of the tank , that is, when working, the heated nitrogen flow is directed towards the liquid surface to help the ethyl formate vaporize.

本发明所述甲酸乙酯稀释混合释放单元的主要作用在于使氮气和甲酸乙酯的混合气体定量与来自熏蒸空间的空气在防爆空间内混合稀释,稀释至安全浓度的甲酸乙酯气体进入熏蒸空间,完成投药。The main function of the ethyl formate dilution mixing release unit in the present invention is to mix and dilute the mixed gas of nitrogen and ethyl formate quantitatively with the air from the fumigation space in the explosion-proof space, and the ethyl formate gas diluted to a safe concentration enters the fumigation space , to complete the dosing.

从上可知,本发明是在氮气环境下,以氮气为保护气,使用加热元件加热甲酸乙酯至沸腾,采用氮气携带气化的甲酸乙酯进入预混合罐体(防爆),进入的氮气和甲酸乙酯的混合气体与来自熏蒸空间的空气在防爆空间内混合稀释(可定量混合),稀释至安全浓度的甲酸乙酯气体(90g/m3以下的甲酸乙酯气体)进入熏蒸空间,完成投药。该系统具有气化迅速、使用经济、操作安全等优势,在水果熏蒸中极具应用前景。As can be seen from above, the present invention is under nitrogen environment, with nitrogen as protection gas, uses heating element to heat ethyl formate to boiling, adopts nitrogen to carry vaporized ethyl formate into premixed tank body (explosion-proof), the nitrogen of entering and The mixed gas of ethyl formate and the air from the fumigation space are mixed and diluted in the explosion-proof space (quantitative mixing is possible), and the ethyl formate gas diluted to a safe concentration (ethyl formate gas below 90g/m 3 ) enters the fumigation space to complete Dosing. The system has the advantages of rapid gasification, economical use, and safe operation, and has great application prospects in fruit fumigation.

作为前述甲酸乙酯投药系统的一具体实施方式,优选地,在所述循环空气进口或混合气体出口与所述熏蒸空间的连接管路上设有密闭风机,以加速混合气体的输出及循环空气的输入。该密闭风机的主要作用是负责把熏蒸空间内的空气送入稀释混合单元,再循环入集装箱或其他熏蒸空间,以保证投药过程中甲酸乙酯可均匀分布在集装箱其他熏蒸空间内部。As a specific implementation of the aforementioned ethyl formate dosing system, preferably, an airtight fan is provided on the connecting pipeline between the circulating air inlet or the mixed gas outlet and the fumigation space, so as to accelerate the output of the mixed gas and the circulation of the circulating air. enter. The main function of the airtight fan is to send the air in the fumigation space into the dilution and mixing unit, and recirculate it into the container or other fumigation spaces, so as to ensure that the ethyl formate can be evenly distributed in other fumigation spaces of the container during the dosing process.

作为前述甲酸乙酯投药系统的一具体实施方式,优选地,所述氮气源包括制氮机或氮气钢瓶。As a specific embodiment of the aforementioned ethyl formate dosing system, preferably, the nitrogen source includes a nitrogen generator or a nitrogen cylinder.

作为前述甲酸乙酯投药系统的一具体实施方式,优选地,所述加热模块为陶瓷发热元件加热模块(PTC加热模块);优选地,其设于所述具不锈钢内壁的罐体的底部,其配有过热终止加热设计;更优选地,该陶瓷发热元件加热模块与液体甲酸乙酯接触的换热面积不低于300cm2,加热功率为3~6Kw,极限加热温度不高于180℃。As a specific embodiment of the aforementioned ethyl formate dosing system, preferably, the heating module is a ceramic heating element heating module (PTC heating module); preferably, it is arranged at the bottom of the tank body with a stainless steel inner wall, and Equipped with an overheating termination heating design; more preferably, the heat exchange area of the ceramic heating element heating module in contact with liquid ethyl formate is not less than 300cm 2 , the heating power is 3-6Kw, and the limit heating temperature is not higher than 180°C.

本发明PTC加热模块为现有技术。采用PTC加热模块一方面可防止过热产生的不安全因素,温度超过180℃自动终止加热;另一方面也可以保证全部液态甲酸乙酯均能气化,在甲酸乙酯气化过程中,PTC温度只能加热至甲酸乙酯的沸点温度55℃左右,只有全部气化后,PTC温度才能进一步上升,因此可以用PTC温度指示气化是否全部完成。The PTC heating module of the present invention belongs to the prior art. The PTC heating module can prevent unsafe factors caused by overheating, and automatically stop heating when the temperature exceeds 180°C; on the other hand, it can also ensure that all liquid ethyl formate can be vaporized. During the gasification process of ethyl formate, the PTC temperature It can only be heated to about 55°C, the boiling point of ethyl formate. Only after it is completely vaporized, the PTC temperature can rise further, so the PTC temperature can be used to indicate whether the gasification is completely completed.

作为前述甲酸乙酯投药系统的一具体实施方式,优选地,所述具不锈钢内壁的罐体还设有残渣排放口。设置该残渣排放口可方便将加热液体甲酸乙酯后的残渣排出。As a specific implementation of the aforementioned ethyl formate dosing system, preferably, the tank body with a stainless steel inner wall is also provided with a residue discharge port. Setting the residue discharge port can facilitate the discharge of the residue after heating the liquid ethyl formate.

作为前述甲酸乙酯投药系统的一具体实施方式,优选地,所述氮气进口还配有气体流量计。As a specific implementation of the aforementioned ethyl formate dosing system, preferably, the nitrogen inlet is also equipped with a gas flow meter.

作为前述甲酸乙酯投药系统的一具体实施方式,优选地,所述甲酸乙酯气体进口和所述循环空气进口分别配有气体流量计。As a specific implementation of the aforementioned ethyl formate dosing system, preferably, the ethyl formate gas inlet and the circulating air inlet are respectively equipped with gas flow meters.

为了方便实际控制需要,本发明还可在所述投药系统中其他位置设置相应的阀门和流量计。In order to facilitate actual control needs, the present invention can also set corresponding valves and flow meters at other positions in the drug delivery system.

本发明采用了如下手段保证工作过程中的安全:The present invention has adopted following means to guarantee safety in the working process:

(1)本发明在投药前,预先使用氮气充满管路;(1) The present invention uses nitrogen to fill the pipeline in advance before dosing;

(2)采用具有过热保护设计PTC加热模块,温度超过180℃自动终止加热。(2) PTC heating module with overheating protection design is adopted, and the heating is automatically terminated when the temperature exceeds 180°C.

(3)甲酸乙酯气化后,在防爆空间内,经过定量稀释,至安全浓度,才进入熏蒸空间。(3) After the ethyl formate is gasified, it is diluted quantitatively in the explosion-proof space to a safe concentration before entering the fumigation space.

综上可知,本发明提供了用于水果熏蒸的甲酸乙酯投药系统及方法,其具有可直接使用液态的甲酸乙酯、气化迅速(气化和投药时间可控制在20min以内)、使用经济及操作安全等优势。In summary, the present invention provides an ethyl formate dosing system and method for fruit fumigation, which has the ability to directly use liquid ethyl formate, rapid gasification (gasification and dosing time can be controlled within 20min), economical to use and operational safety.

附图说明Description of drawings

图1为本发明实施例1提供的用于水果熏蒸的甲酸乙酯投药系统的示意图,图中标号具有如下意义:Fig. 1 is the schematic diagram of the ethyl formate dosing system that is used for fruit fumigation that the embodiment of the present invention 1 provides, and label among the figure has following meaning:

1:氮气供应单元;2:气体加热器;3:氮气进口;4:液体甲酸乙酯进口;5:甲酸乙酯气化单元;6:PTC加热模块;7:残渣排放口;8:甲酸乙酯气体出口;9:甲酸乙酯稀释混合释放单元;10:混合气体出口;11:循环空气进口;12:密闭风机;13:集装箱。1: nitrogen supply unit; 2: gas heater; 3: nitrogen inlet; 4: liquid ethyl formate inlet; 5: ethyl formate gasification unit; 6: PTC heating module; 7: residue discharge port; 8: ethyl formate Ester gas outlet; 9: ethyl formate dilution mixed release unit; 10: mixed gas outlet; 11: circulating air inlet; 12: airtight fan; 13: container.

具体实施方式detailed description

为了对本发明的技术特征、目的和有益效果有更加清楚的理解,现结合具体实施例及对本发明的技术方案进行以下详细说明,应理解这些实例仅用于说明本发明而不用于限制本发明的范围。实施例中,各原始试剂材料均可商购获得,未注明具体条件的实验方法为所属领域熟知的常规方法和常规条件,或按照仪器制造商所建议的条件。In order to have a clearer understanding of the technical features, purposes and beneficial effects of the present invention, now in conjunction with specific embodiments and the technical solutions of the present invention are described in detail below, it should be understood that these examples are only used to illustrate the present invention and are not intended to limit the scope of the present invention scope. In the examples, each original reagent material can be obtained commercially, and the experimental methods without specific conditions are conventional methods and conventional conditions well known in the art, or according to the conditions suggested by the instrument manufacturer.

实施例1Example 1

本实施例提供一种用于水果熏蒸的甲酸乙酯投药系统及方法,请参阅图1,其为该甲酸乙酯投药系统的示意图,其包括氮气供应单元1、甲酸乙酯气化单元5及甲酸乙酯稀释混合释放单元9;The present embodiment provides a kind of ethyl formate dosing system and method for fruit fumigation, please refer to Fig. 1, it is the schematic diagram of this ethyl formate dosing system, it comprises nitrogen supply unit 1, ethyl formate gasification unit 5 and Ethyl formate dilution mixed release unit 9;

所述氮气供应单元1包括氮气源及氮气出口;Described nitrogen supply unit 1 comprises nitrogen source and nitrogen outlet;

所述甲酸乙酯气化单元5包括具不锈钢内壁的罐体,体积为5L,在该罐体上设有液体甲酸乙酯进口4、氮气进口3、甲酸乙酯气体出口8及残渣排放口7;所述氮气进口3垂直朝向该罐体的底部,其通过管路与所述氮气出口相连,位于工作时甲酸乙酯液面上方;该罐体还设有用于加热液体甲酸乙酯的PTC加热模块6;该PTC加热模块6设于所述具不锈钢内壁的罐体的底部;该PTC加热模块6与液体甲酸乙酯接触的换热面积350cm2,加热功率3.5Kw,其配有过热终止加热设计,极限加热温度130℃。Described ethyl formate gasification unit 5 comprises the tank body of tool stainless steel inner wall, volume is 5L, is provided with liquid ethyl formate inlet 4, nitrogen gas inlet 3, ethyl formate gas outlet 8 and residue discharge port 7 on this tank body ; The nitrogen inlet 3 is vertically towards the bottom of the tank, and it is connected with the nitrogen outlet through a pipeline, above the liquid level of ethyl formate during work; the tank is also provided with a PTC heating for heating liquid ethyl formate Module 6; the PTC heating module 6 is located at the bottom of the tank body with a stainless steel inner wall; the heat exchange area of the PTC heating module 6 in contact with liquid ethyl formate is 350cm 2 , the heating power is 3.5Kw, and it is equipped with overheating termination heating Design, the limit heating temperature is 130°C.

所述甲酸乙酯稀释混合释放单元9包括具有防爆设计的不锈钢罐体,体积为100L,在该罐体上设有甲酸乙酯气体进口、循环空气进口11及混合气体出口10;所述甲酸乙酯气体进口通过管路与所述甲酸乙酯气体出口8相连;该循环空气进口11及该混合气体出口10分别通过管路与集装箱13的熏蒸空间连通,以将该稀释混合后的混合气体输入到该熏蒸空间,及将该熏蒸空间的空气循环输入该不锈钢罐体内;Described ethyl formate dilution mix release unit 9 comprises the stainless steel tank body with explosion-proof design, and volume is 100L, is provided with ethyl formate gas inlet, circulating air inlet 11 and mixed gas outlet 10 on this tank body; The ester gas inlet is connected to the ethyl formate gas outlet 8 through a pipeline; the circulating air inlet 11 and the mixed gas outlet 10 are respectively communicated with the fumigation space of the container 13 through a pipeline, so that the diluted mixed gas is input to the fumigation space, and to circulate air from the fumigation space into the stainless steel tank;

在所述混合气体出口10与所述熏蒸空间的连接管路上设有密闭风机12,以加速混合气体的输出及循环空气的输入;An airtight fan 12 is provided on the connecting pipeline between the mixed gas outlet 10 and the fumigation space to accelerate the output of the mixed gas and the input of circulating air;

在所述氮气出口与所述氮气进口3的连接管路上还设有用于加热氮气的气体加热器2;所述氮气源为氮气钢瓶;A gas heater 2 for heating nitrogen is also provided on the connecting pipeline between the nitrogen outlet and the nitrogen inlet 3; the nitrogen source is a nitrogen cylinder;

在所述氮气进口3、甲酸乙酯气体进口及循环空气进口11分别还配有气体流量计(图中未示出)。The nitrogen gas inlet 3, the ethyl formate gas inlet and the circulating air inlet 11 are respectively equipped with gas flow meters (not shown in the figure).

在上述各进口或出口处还设有控制物料进出的阀门。There are also valves to control the entry and exit of materials at the above-mentioned inlets or outlets.

应用前述的甲酸乙酯投药系统的方法包括如下步骤:The method for applying the aforementioned ethyl formate dosing system may further comprise the steps:

开启所述氮气单元向整个所述甲酸乙酯投药系统内供应氮气;Open the nitrogen unit to supply nitrogen to the entire ethyl formate dosing system;

从所述液体甲酸乙酯进口4向所述具不锈钢内壁的罐体内供应3L液体甲酸乙酯,通过所述PTC加热模块6加热液体甲酸乙酯使其气化,气化后的甲酸乙酯气体在氮气的携带下从所述甲酸乙酯气体出口8进入所述甲酸乙酯稀释混合释放单元9,然后与来自于集装箱13的熏蒸空间的空气混合稀释,最后从所述混合气体出口10进入熏蒸空间。From the liquid ethyl formate inlet 4, 3L liquid ethyl formate is supplied to the tank with stainless steel inner wall, and the liquid ethyl formate is heated by the PTC heating module 6 to make it gasified, and the gasified ethyl formate gas Enter the ethyl formate dilution mixing release unit 9 from the ethyl formate gas outlet 8 under the carrying of nitrogen, then mix and dilute with the air from the fumigation space of the container 13, and finally enter the fumigation from the mixed gas outlet 10 space.

通过气体流量计控制供应氮气的流速控制在200L/min,供应的氮气经气体加热器2加热,该气体加热器的功率为1.5Kw,被加热后的氮气温度135℃。The flow rate of the supplied nitrogen is controlled at 200 L/min by a gas flow meter, and the supplied nitrogen is heated by a gas heater 2 whose power is 1.5Kw, and the temperature of the heated nitrogen is 135°C.

在10min内,液体甲酸乙酯气化完毕。Within 10 min, the vaporization of liquid ethyl formate was complete.

控制甲酸乙酯气体进口气量/循环空气进口气量=1/20,经检测所述混合气体出口10甲酸乙酯的浓度在65g/m3。甲酸乙酯的浓度检测使用配有火炎离子检测器(FID)的气相色谱进行,通过外标法计算样品中的甲酸乙酯浓度。先将200g/m3甲酸乙酯标准气体稀释至不同浓度,绘制标准曲线,再根据标准曲线计算样品中甲酸乙酯的准确浓度。气相色谱条件:进样口温度:220℃,填充色谱柱Propark Q(80-100目),柱温:80℃,FID:250℃,载气:H2,N2,柱流量:40mL/min,参比气流量:50mL/min。Control ethyl formate gas inlet gas volume/circulating air inlet gas volume=1/20, and the concentration of ethyl formate at the outlet 10 of the mixed gas is detected to be 65g/m 3 . The detection of the concentration of ethyl formate was carried out using a gas chromatograph equipped with a flame ionization detector (FID), and the concentration of ethyl formate in the sample was calculated by the external standard method. First dilute 200g/m 3 ethyl formate standard gas to different concentrations, draw a standard curve, and then calculate the exact concentration of ethyl formate in the sample according to the standard curve. Gas chromatography conditions: inlet temperature: 220°C, packed column Propark Q (80-100 mesh), column temperature: 80°C, FID: 250°C, carrier gas: H 2 , N 2 , column flow: 40mL/min , Reference gas flow: 50mL/min.

对比例1Comparative example 1

本对比例与实施例1基本相同,不同之处仅是氮气进口为水平朝向,且不对氮气进行加热,按实施例1相同的方式操作,实验表明相同体积的甲酸乙酯需要40min才可气化完毕。这大大延长了投药时间。This comparative example is basically the same as in Example 1, except that the nitrogen inlet is horizontally oriented, and the nitrogen is not heated, and it is operated in the same manner as in Example 1. Experiments show that the same volume of ethyl formate needs 40 minutes to be vaporized complete. This greatly prolongs the dosing time.

最后说明的是:以上实施例仅用于说明本发明的实施过程和特点,而非限制本发明的技术方案,尽管参照上述实施例对本发明进行了详细说明,本领域的普通技术人员应当理解:依然可以对本发明进行修改或者等同替换,而不脱离本发明的精神和范围的任何修改或局部替换,均应涵盖在本发明的保护范围当中。Finally, it is explained that the above examples are only used to illustrate the implementation process and characteristics of the present invention, rather than limiting the technical solution of the present invention. Although the present invention has been described in detail with reference to the above examples, those of ordinary skill in the art should understand that: The present invention can still be modified or equivalently replaced, and any modification or partial replacement that does not depart from the spirit and scope of the present invention shall be covered by the protection scope of the present invention.

Claims (10)

1. a kind of Ethyl formate medication administration method fumigated for fruit, methods described use Ethyl formate administration system, the formic acid Ethyl ester administration system includes nitrogen supply (NS) unit, Ethyl formate gasification unit and Ethyl formate dilution mixing releasing unit;
The nitrogen supply (NS) unit includes source nitrogen and nitrogen outlet;
The Ethyl formate gasification unit includes the tank body of tool stainless steel inwall, enters on the tank body provided with liquid Ethyl formate Mouth, nitrogen inlet and Ethyl formate gas vent;The bottom of the nitrogen inlet vertically tank body, it passes through pipeline and institute State nitrogen outlet to be connected, Ethyl formate ullage during positioned at work;The tank body is additionally provided with for heating liquid Ethyl formate Heating module;
The Ethyl formate dilution mixing releasing unit includes the stainless steel tank body with Explosion-proof Design, and first is provided with the tank body Acetoacetic ester gas feed, circulation air import and mixed gas outlet;The Ethyl formate gas feed by pipeline with it is described Ethyl formate gas vent is connected;The circulation air import and the mixed gas outlet by pipeline and hold thing to be fumigated respectively The stifling space connection of container, the mixed mixed gas of the dilution is input to the stifling space, and this is fumigated into space Air circulation input in the stainless cylinder of steel body;The Ethyl formate medication administration method comprises the following steps:
Open nitrogen unit the supply of nitrogen into the whole Ethyl formate administration system;
Liquid Ethyl formate is supplied into the tank body of the tool stainless steel inwall from the liquid Ethyl formate import, by described Heating module heating liquid Ethyl formate is vaporized, and the Ethyl formate gas after gasification is under the carrying of nitrogen from the formic acid Ethyl ester gas vent enters Ethyl formate dilution mixing releasing unit, then holds the smoked of thing container to be fumigated with coming from The air mixed diluting in space is steamed, finally enters stifling space from the mixed gas outlet;
Control Ethyl formate gas feed tolerance/circulation air import tolerance=1/20 so that the mixed gas outlet formic acid The concentration of ethyl ester is in 60~80g/m3
The flow control of the supply of nitrogen is in 190~250L/min;
The gas heater for heated nitrogen is additionally provided with the nitrogen outlet and the connecting line of the nitrogen inlet;For The nitrogen answered heats through the gas heater, and the power of the gas heater is 1~3Kw, the nitrogen temperature 130 after being heated ~150 DEG C.
2. Ethyl formate medication administration method according to claim 1, wherein, go out in the circulation air import or mixed gas Mouthful and the connecting line in the stifling space be provided with closed blower fan, to accelerate the defeated of the output of mixed gas and circulation air Enter.
3. Ethyl formate medication administration method according to claim 1, wherein, the heating module heats for ceramic heating element Module;Preferably, it is located at the bottom of the tank body of the tool stainless steel inwall, and it is equipped with overheat termination heating design;More preferably Ground, the heat exchange area that the ceramic heating element heating module contacts with liquid Ethyl formate are not less than 300cm2, heating power 3 ~6Kw, limit heating-up temperature are not higher than 180 DEG C.
4. Ethyl formate medication administration method according to claim 1, wherein, the tank body for having stainless steel inwall is additionally provided with residual Slag floss hole.
5. Ethyl formate medication administration method according to claim 1, wherein, the nitrogen inlet is also equipped with gas flowmeter; The Ethyl formate gas feed and the circulation air import are respectively provided with gas flowmeter.
6. a kind of Ethyl formate administration system fumigated for fruit, wherein, the Ethyl formate administration system includes nitrogen supply (NS) Unit, Ethyl formate gasification unit and Ethyl formate dilution mixing releasing unit;
The nitrogen supply (NS) unit includes source nitrogen and nitrogen outlet;
The Ethyl formate gasification unit includes the tank body of tool stainless steel inwall, enters on the tank body provided with liquid Ethyl formate Mouth, nitrogen inlet and Ethyl formate gas vent;The bottom of the nitrogen inlet vertically tank body, it passes through pipeline and institute State nitrogen outlet to be connected, Ethyl formate ullage during positioned at work;The tank body is additionally provided with for heating liquid Ethyl formate Heating module;
The Ethyl formate dilution mixing releasing unit includes the stainless steel tank body with Explosion-proof Design, and first is provided with the tank body Acetoacetic ester gas feed, circulation air import and mixed gas outlet;The Ethyl formate gas feed by pipeline with it is described Ethyl formate gas vent is connected;The circulation air import and the mixed gas outlet by pipeline and hold thing to be fumigated respectively The stifling space connection of container, the mixed mixed gas of the dilution is input to the stifling space, and this is fumigated into space Air circulation input in the stainless cylinder of steel body;
The gas heater for heated nitrogen is additionally provided with the nitrogen outlet and the connecting line of the nitrogen inlet;
Preferably, the nitrogen inlet is also equipped with gas flowmeter;
Preferably, the Ethyl formate gas feed and the circulation air import are respectively provided with gas flowmeter.
7. the Ethyl formate administration system according to claim 6 fumigated for fruit, wherein, the source nitrogen includes system Nitrogen machine or nitrogen cylinder.
8. the Ethyl formate administration system according to claim 6 fumigated for fruit, wherein, the tool stainless steel inwall Tank body be additionally provided with residue floss hole.
9. the Ethyl formate administration system according to claim 6 fumigated for fruit, wherein, enter in the circulation air Mouthful or the connecting line in mixed gas outlet and the stifling space be provided with closed blower fan, with accelerate the output of mixed gas and The input of circulation air.
10. the Ethyl formate administration system according to claim 9 fumigated for fruit, wherein, the heating module is Ceramic heating element heating module;Preferably, it is located at the bottom of the tank body of the tool stainless steel inwall, and it is equipped with overheat termination Heating design;It is highly preferred that the ceramic heating element heating module is not less than with the heat exchange area that liquid Ethyl formate contacts 300cm2, heating power is 3~6Kw, and limit heating-up temperature is not higher than 180 DEG C.
CN201710873109.XA 2017-09-25 2017-09-25 A kind of Ethyl formate administration system fumigated for fruit and method Pending CN107549299A (en)

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1260111A (en) * 1997-03-18 2000-07-19 波克股份有限公司 Gas-fumigation disinfecting method and system
CN101146445A (en) * 2005-03-24 2008-03-19 德克勒恩比利时股份有限公司 Method and apparatus for fumigation of products in enclosed spaces
CN102960327A (en) * 2012-11-19 2013-03-13 中国检验检疫科学研究院 Intelligent fumigation system of living plant and application of intelligent fumigation system
CN104604835A (en) * 2015-02-16 2015-05-13 江西省瑞翔卫生处理技术服务有限公司 Intelligent fumigating system
CN105876590A (en) * 2014-09-10 2016-08-24 中国检验检疫科学研究院 Novel ethyl formate quantitative dosing system
CN207613115U (en) * 2017-09-25 2018-07-17 中国检验检疫科学研究院 A kind of Ethyl formate administration system fumigated for fruit

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1260111A (en) * 1997-03-18 2000-07-19 波克股份有限公司 Gas-fumigation disinfecting method and system
CN101146445A (en) * 2005-03-24 2008-03-19 德克勒恩比利时股份有限公司 Method and apparatus for fumigation of products in enclosed spaces
CN102960327A (en) * 2012-11-19 2013-03-13 中国检验检疫科学研究院 Intelligent fumigation system of living plant and application of intelligent fumigation system
CN105876590A (en) * 2014-09-10 2016-08-24 中国检验检疫科学研究院 Novel ethyl formate quantitative dosing system
CN104604835A (en) * 2015-02-16 2015-05-13 江西省瑞翔卫生处理技术服务有限公司 Intelligent fumigating system
CN207613115U (en) * 2017-09-25 2018-07-17 中国检验检疫科学研究院 A kind of Ethyl formate administration system fumigated for fruit

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