FLOODED JET OF SELF-FOAMING GAS-AEROSOL FOAM WHEN EXTINGUISHING PETROLEUM PRODUCT FIRES IN TANKS BY SUB-LAYER METHOD

Николай Петрович Копылов, Дмитрий Вячеславович Федоткин, Е.Ю. Сушкина, Е.А. Москвилин
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Abstract

Тушение пожаров нефтепродуктов в резервуарах с использованием технологии получения самовспенивающейся газоаэрозоленаполненной пены и подачей ее в слой горючего является наиболее перспективным направлением. В статье проанализированы методы расчета осевой скорости турбулентной затопленной струи в жидкости. Эти методы базируются на решении уравнений Навье-Стокса с привлечением экспериментальных данных. Выполнен расчет осевой скорости струи по разным формулам и для различных уровней взлива нефтепродуктов. Получена хорошая сходимость результатов расчетов и экспериментальных данных. Under-layer extinguishing of petroleum product fires in tanks is widely used in practice, but has a number of significant drawbacks – dissolution of foam in alcohol-containing fuels, failure to penetrate the water cushion and strongly heated layer of fuel. A new extinguishing technology using the technology of self-foaming gas-aerosol foam (SGF) allows to overcome the noted disadvantages of the classical method of under-layer extinguishing. According to this technology, the foam is supplied in the form of a flooded turbulent jet, flowing from a pipe in the base of the tank. The maximum height of the tank, according to modern standards, is 18 meters. The question arises as to what parameters a turbulent flood jet will penetrate the oil product layer and spread over the surface of the tank mirror. The motion of a flooded turbulent jet in a liquid is described by a system of Navier-Stokes equations. This system can be solved analytically with some assumptions or numerically. When solving this problem, some coefficients appear, which, as a rule, are determined experimentally. In this article, various approaches to solving the Navier-Stokes equations for determining the axial velocity of a turbulent flooded jet are considered in the axisymmetric formulation. Calculation formulas and values of empirical constants are determined. The calculation of velocity values on the axis of turbulent flooded jet has been carried out for values of its initial velocity U0 = 35 m ∙ s–1 and pipe diameter D0 = 0,159 m, through which the stream flows out. The values of these parameters are realized in practice in the installation “Uragan”, which implements the technology of obtaining SGF. The calculation results were compared with the data obtained in natural experiments, their good agreement was obtained. As a result, it has been experimentally and computationally proved that the new technology of sub-layer fire extinguishing of SGF is effective.
采用分层法扑灭储罐中的石油产品火灾时,自发泡气体-气溶胶泡沫的淹没射流
Тушение пожаров нефтепродуктов в резервуарах с использованием технологии получения самовспенивающейсягазоаэрозоленаполненной пены и подачей ее в слой горючего является наиболее перспективным направлением.В статье проанализированы методы расчета осевой скорости турбулентной затопленной струи в жидкости.Эти методы базируются на решении уравнений Навье-Стокса с привлечением экспериментальных данных.Выполнен расчет осевой скорости струи по разным формулам и для различных уровней взлива нефтепродуктов.在熄灭过程中,应注意以下几点: 1. 储油罐中石油产品火灾的底层灭火在实践中得到广泛应用,但也存在一些重大缺陷--泡沫会溶解在含酒精的燃料中,无法穿透水垫和受热强烈的燃料层。使用自发泡气体-气溶胶泡沫(SGF)技术的新型灭火技术可以克服传统层下灭火方法的缺点。根据该技术,泡沫以淹没式湍流喷射的形式供应,从罐体底部的管道流出。根据现代标准,水箱的最大高度为 18 米。由此产生的问题是,湍流洪流在多大参数下才能穿透油品层并在油罐镜面上扩散。液体中的湍流洪流运动由纳维-斯托克斯方程组描述。该方程组可以在某些假设条件下通过分析或数值方法求解。在求解这个问题时,会出现一些系数,而这些系数通常是通过实验确定的。本文考虑了在轴对称形式下求解纳维-斯托克斯方程的各种方法,以确定湍流淹没射流的轴向速度。确定了计算公式和经验常数值。湍流泛流射流轴向速度值的计算是在其初始速度 U0 = 35 m ∙ s-1 和管道直径 D0 = 0,159 m 的条件下进行的。这些参数值是在 "Uragan "装置中实际实现的,该装置采用了获取 SGF 的技术。计算结果与自然实验中获得的数据进行了比较,结果一致。因此,实验和计算证明,SGF 底层灭火新技术是有效的。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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