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Ozone Model for Drip Irrigation Systems

机译:滴灌仪表灌溉系统

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摘要

Ozone concentration was modeled along a subsurface drip irrigation system. The project generated two models; a model with two-phase flow with ozone in the gas and liquid phases within the tube, and a model with single-phase flow using only aqueous ozone. The equilibrium concentrations of ozone in the gas and liquid phases were calculated with Henry's Law. The models were evaluated with field experiments in which ozone was produced and injected into a drip irrigation system. In order to obtain a control measurement, in some experiments, ozone gas was removed prior to the drip irrigation tube by a degasser. Three water qualities were used in the experiments, potable water with chlorine, open storage tank water with high organic matter concentration, and open storage tank water with low organic matter concentration. Water was collected every 10 m along the irrigation system and aqueous ozone concentration was measured. The best-fit degradation coefficient for potable water was 0.003/s, and for storage tank water (for both high and low organic matter concentrations) was 0.004/s. This ozone model could be used in the field to calculate the required ozone production rate and concentration at the injector in order to maintain an acceptable concentration at end of the irrigation system.
机译:臭氧浓度沿着地下滴灌系统进行建模。该项目产生了两种型号;一种模型,具有两相流的臭氧,在管内的气体和液相中,以及仅使用臭氧水溶液的单相流的模型。用亨利法律计算了气体和液相中臭氧的平衡浓度。用现场实验评估模型,其中产生臭氧并注入滴灌系统。为了获得对照测量,在一些实验中,通过脱气剂在滴灌管之前除去臭氧气体。实验中使用三种水质,饮用水用氯,开放储罐水,具有高有机物质浓度,并具有低有机物质浓度的储罐水。每10米沿着灌溉系统收集水,并测量含水臭氧水溶液。饮用水的最佳拟合降解系数为0.003 / s,并且对于储罐水(高有机物质浓度)为0.004 / s。该臭氧模型可用于该领域,以计算喷射器所需的臭氧生产速率和浓度,以便在灌溉系统结束时保持可接受的浓度。

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