宋海潮, 徐幼林, 郑加强, 汪希伟, 张敏. 脂溶性农药旋动射流混药器结构分析与混合均匀性试验[J]. 农业工程学报, 2016, 32(23): 86-92. DOI: 10.11975/j.issn.1002-6819.2016.23.012
    引用本文: 宋海潮, 徐幼林, 郑加强, 汪希伟, 张敏. 脂溶性农药旋动射流混药器结构分析与混合均匀性试验[J]. 农业工程学报, 2016, 32(23): 86-92. DOI: 10.11975/j.issn.1002-6819.2016.23.012
    Song Haichao, Xu Youlin, Zheng Jiaqiang, Wang Xiwei, Zhang Min. Structural analysis and mixing uniformity experiments of swirling jet mixer for applying fat-soluble pesticides[J]. Transactions of the Chinese Society of Agricultural Engineering (Transactions of the CSAE), 2016, 32(23): 86-92. DOI: 10.11975/j.issn.1002-6819.2016.23.012
    Citation: Song Haichao, Xu Youlin, Zheng Jiaqiang, Wang Xiwei, Zhang Min. Structural analysis and mixing uniformity experiments of swirling jet mixer for applying fat-soluble pesticides[J]. Transactions of the Chinese Society of Agricultural Engineering (Transactions of the CSAE), 2016, 32(23): 86-92. DOI: 10.11975/j.issn.1002-6819.2016.23.012

    脂溶性农药旋动射流混药器结构分析与混合均匀性试验

    Structural analysis and mixing uniformity experiments of swirling jet mixer for applying fat-soluble pesticides

    • 摘要: 以研究乳油、悬乳剂等脂溶性农药在线混药均匀性为目的,基于产品结构分析旋动射流混药器的混合机理,并提出提高混药器混合效率的措施:继旋器起旋、螺旋收缩管、分流器切向径流和在扩散管中增加导叶等方式提高混合液旋动效率。研究了这些措施对在线射流混药器混合效果的影响。为了提高旋转效率,减少阻力损失,继旋器内设有3个导叶,导叶高度6.5 mm,导叶包角15°;扩散管内导叶高度由0逐渐增加到6.5 mm,导叶包角15°;分流器进药采用切向进入,切向角β根据农药黏度、浓度等不同而改变;收缩管收缩度为0.095,收缩管螺距128 mm,收缩角16°。经过数值仿真,水和农药能够实现螺旋状流动,喷头处药液容积分数分布均匀性指数为0.999 5,药液分布一致。试验结果发现:旋动射流混药器出口与喷头直接连接时,农药需要药泵注药才能实现在线混合;混药器出口最大混合比为99.442 5%,旋动射流混药器能够实现脂溶性农药和水均匀混合。

       

      Abstract: Abstract: The on-line pesticide mixing is a process with higher productivity and safer operating conditions, which can reduce pesticide wastes and pollution. To characterize jet mixing characteristics for on-line injection of pesticides, a new mixing device based on the swirling jet mechanism was conceived and developed to improve the mixing uniformity of water and fat-soluble pesticides. The swirl jet mixer consisted of a spiral curved shrink tube, a diffuser and a spiral flow generator, and could accelerate the two-phase flow's spiral movement and blend the 2 kinds of liquids. In order to increase the swirling efficiency of swirling jet mixer, the spiral flow generator had 3 guide vanes (height was 6.5 mm, wrap angle was 15°); the diffuser had also 3 guide vanes, but its height was from 0 to 6.5 mm; the pitch of the spiral curved shrink tube was 128 mm, and its converging angle was 16°. A computational fluid dynamics program (FLUENT) was used to simulate the flow field inside the swirling jet mixer to optimize its design. The boundary conditions of the water and the rapeseed oil were defined to a pressure input. The boundary condition of mixer outlet was defined to a pressure output. The total gauge pressure, the initial gauge pressure and the turbulence intensity were defined. The solid wall was supposed to be a non-slip, impervious and adiabatic boundary. The segregated and implicit modeling was identified by incompressible fluid. The steady flow and the k-??modeling of turbulent flow were identified. The mixing uniformity was evaluated by introducing the uniformity index, and the 2 kinds of liquids were blended homogenously as the uniformity index was 1. Simulation results showed that the uniformity index was 0.999 5 across the entire cross sections inside the mixer, confirming the uniform mixture characteristics with the new mixer design. To verify the simulation results, the experiments were conducted in which the fluorescent tracers were mixed with the pesticides to enable the camera to track the mixing process in the transparent chamber. The mixing process in the on-line injection system actually is a process that water from the water tank and pesticide from the pesticide tank are mixed in the mixer through the liquid convection and pervasion. Water was set as the main flow phase, with the density of 1.0 g/cm3, the kinematic viscosity of 1 mm2/s and the surface tension of 72 mN/m. The rapeseed oil was set as the second flow phase, with the density of 0.9 g/cm3, the kinematic viscosity of 43 mm2/s and the surface tension of 29.8 mN/m. The mixing experimental system for the mixer included water intake system, pesticide intake system and image acquisition system. The water intake system contained water tank, water pump, water flowmeter, water manometer and water piezometer, while the pesticide intake system contained pesticide tank, pesticide pump, pesticide flowmeter, pesticide manometer and pesticide piezometer. The water and the pesticide were mixed straightway by the pesticide mixer before they were sprayed by a nozzle. The experimental results showed that the pressures of the water piezometer, the pesticide piezometer and the outlet of the mixer were separately 0.23, 0.22 and 0.22 MPa. The maximum mixing ratio was 99.442 5% at the outlet of the mixer, so the mixer had significant uniformity index for the fat-soluble pesticide. The simulations and the verification tests indicated that the mixing uniformity was very good in the swirling jet mixer when applying fat-soluble pesticides through on-line injection spray. Therefore, the new swirling jet mixer would solve the non-uniform mixture problem associated with conventional mixers and could significantly improve the on-line injection technology to reduce pesticide waste. The swirling jet mixer was desirable, and its structure was compact. Furthermore, there were mandatory and optional items, and we could choose what we needed according to the spraying conditions. It is conducive to the application and marketing promotion of the plant protection machineries.

       

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