scholarly journals Efficiency of fire extinguishing with general purpose fire extinguishing powder in case of non-stationary interaction of its particles with burning material

Author(s):  
A. I. Kitsak

Evaluation of the effectiveness of fire extinguishing by jet systems of powder fire extinguishing in conditions of non-stationary heat exchange processes and heterogeneous inhibition of active flame centers by powder particles was the aim of the work. The theoretical dependence of the amount of heat, absorbed by the particles of fire extinguishing powder, and the reaction rate of heterogeneous active centers of flame, inhibiting them, in non-stationary conditions of heat transfer, as well as inhibition reaction for fire extinguishing ink jet systems were obtained. The extinguishing of a flame with a fire extinguishing powder under non-stationary conditions is more effective, the smaller is the effective size of the powder particles, the longer is their stay in the combustion zone, and the shorter are the characteristic times of heat transfer and inhibition reaction. Comparison of the estimates of the characteristic duration of heat transfer and inhibition reaction for widely used fire extinguishing powders has shown a large inertia of the thermal mechanism of fire extinguishing, which greatly reduces its effectiveness at high speeds of powder particles in the combustion zone.

2020 ◽  
pp. 63-70
Author(s):  
Анатолий Ильич Кицак

Предложена модель механизма гетерогенного ингибирования активных центров пламени частицами огнетушащего порошка общего назначения при нестационарном взаимодействии. Проведена оценка эффективности гетерогенного ингибирования активных центров пламени частицами огнетушащего порошка в нестационарном режиме их взаимодействия. Полученные результаты могут быть использованы для оптимизации условий и режимов подачи огнетушащего порошка в зону горения в целях достижения максимального эффекта тушения пожара. The relevance of the work is due to the need to improve the efficiency of powder fire extinguishing systems. The aim of this work is to evaluate the effectiveness of the mechanism of heterogeneous inhibition of active flame centers by particles of fire extinguishing powder under non-stationary conditions of interaction. It was achieved by the method of theoretical modeling. There are obtained theoretical dependences of the reaction rate of heterogeneous inhibition of active flame centers by fire extinguishing powder particles on their dispersed and dynamic characteristics under non-stationary conditions of active particles interaction with the inhibitor surface. The efficiency of heterogeneous inhibition of active flame centers by fire extinguishing powder particles in a non-stationary mode of their interaction was evaluated. Fire fighting with fire extinguishing powder under non-stationary conditions is more effective the smaller the effective size of powder particles, the effective duration of the inhibition reaction and the longer the interaction time of powder particles with active flame centres. It was established that inhibition efficiency depends either on the kinetic parameters of active centers and disperse characteristics of the powder particles or on the ratio of interaction time of powder particles with the active centers as well as the characteristic duration of inhibition reaction. The results obtained allow optimizing the conditions and modes of fire extinguishing powder supply to the combustion zone in order to achieve the maximum effect of fire extinguishing.


2019 ◽  
Vol 10 (4) ◽  
pp. 391-401
Author(s):  
A. I. Kitsak

The aim of the paper was to develop a model of thermal extinguishing mechanism using dry chemical powder taking into account the inertia of heat transfer to powder particles during unsteady heat exchange to identify the optimal conditions for extinguishing of A1 class fires with powders.The method of experimental and mathematical modelling of fire extinguishing process using dry chemical powder with short-term effect on the fire was used to achieve the goal. The experimental dependences of the extinguishing time and unit consumption of the extinguishing powder on the intensity of the powder supply to the combustion zone in extinguishing of subclass A1 fire in same area and in a limited volume were obtained. The mathematical model of a thermal extinguishing mechanism using dry chemical powder has been developed, taking into account the inertia of heat transfer to powder particles during unsteady heat exchange.Analysis of the regularities of extinguishing the subclass A1 fire using powder with a short feeding it into the fire indicates the presence of optimum values of unity consumption of powder on the fire from the intensity of feeding it into the fire. The presence of this optimum is due to the inertia of extinguishing the subclass A1 fire using powder due to the finiteness of the heat transfer time to the particles of the extinguishing powder and the limited time of interaction of particles with the combustible material.The theoretical analysis of the fire extinguishing process over the area taking into account the inertia of heat transfer to the powder particles at non-stationary heat exchange are carried out. The results of the analysis are in qualitative agreement with the results of the experimental study of the regularities of extinguishing of model fire foci of subclass A1 with General-purpose fire extinguishing powder.


2020 ◽  
Vol 29 (5) ◽  
pp. 89-99
Author(s):  
A. I. Kitsak

Introduction. Presently, there are several problems in the field of dry powder fire suppression that require the indepth study of the physics and technology of fire suppression processes using these substances. One of the ways to find the solution to these problems is the efficiency analysis (theoretical and experimental) of frequently implemented fire extinguishing patterns involving fire suppression systems spraying dry powder, when the term of interaction between the dry fire extinguishing powder and the burning material is close to the duration of principal fire extinguishing patterns, or thermal and heterogeneous inhibition of active flame centres.Purpose and objectives. The purpose of the work was to assess the efficiency of principal fire extinguishing patterns (thermal and heterogeneous inhibition of active flame centres) amid non-stable heat exchange processes and heterogeneous inhibition of active combustion product particles by powder particles.Methods. The pre-set objective was achieved through theoretical modeling of patterns of thermal fire extinguishing and heterogeneous inhibition of active flame centres by dry chemical powder particles.Results. It was established that fire suppression with the help of general purpose dry chemical powder under non-steady conditions is the more effective, the smaller the effective size of powder particles, the longer the time of their stay in the combustion area and the shorter the characteristic period of heat transfer to powder particles and heterogeneous inhibition of active flame centres.Conclusions. The results optimize conditions and patterns of dry fire extinguishing powder application to a combustion area to achieve the highest extinguishing effect and to conduct a targeted search for new dry chemical powders having pre-set thermal and physical specifications.


Author(s):  
Cengiz Camci ◽  
Boris Glezer

The liquid crystal thermography can be successfully used in both transient and steady-state heat transfer experiments with excellent spatial resolution and good accuracy. Although most of the past liquid crystal based heat transfer studies are reported in the stationary frame, measurements from the rotating frame of turbomachinery systems exist The main objective of the present investigation is to determine the influence of rotation on the color calibration of encapsulated liquid crystals sprayed on the flat surface of a rotating aluminum disk. The investigation is performed for a rotational speed range from 0 rpm to 7500 rpm using three different liquid crystal coatings displaying red at 30, 35 and 45° C, under stationary conditions. An immediate observation from the present study is that the color response of liquid crystals is strongly modified by the centrifugal acceleration of the rotating environment. It is consistently and repeatedly observed that the hue versus temperature curve is continuously shifted toward lower temperatures by increasing rotational speed. The relative shift of the display temperature of the green can be as high as 7°C at 7500 rpm when compared to the temperature of the green observed under stationary conditions. The present study shows that relative shift of the liquid crystal color has a well-defined functional dependency to rotational speed. The shift is linearly proportional to the centrifugal acceleration. It is interesting to note that the individual shift curves of the green for all three liquid crystal coatings collapse into a single curve when they are normalized with respect to their own stationary green values. When the color attribute is selected as “intensity” instead of “hue”, very similar shifts of the temperature corresponding to the intensity maximum value appearing around green is observed. An interpretation of the observed color shift is made from a thermodynamics energy balance point of view.


Author(s):  
Will Schreiber ◽  
John Kuo

Abstract The current paper describes a computer model designed to analyze the moisture transport in the unmelted, porous soil neighboring a convecting melt. The time-dependent fluid and heat flow in the soil melt is simulated implicitly using the SIMPLE method generalized to predict viscous fluid motion and heat transfer on boundary-fitted, non-orthogonal coordinates which adapt with time. TOUGH2, a general-purpose computer code for multiphase fluid and heat flow developed by K. Pruess at Lawrence Berkekey Laboratory, has been modified for use on time-adaptive, boundary-fitted coordinates to predict heat transfer, moisture and air transport, and pressure distribution in the porous, unmelted soil. The soil melt model is coupled with the modified TOUGH2 model via an interface (moving boundary) whose shape is determined implicitly with the progression of time. The computer model’s utility is demonstrated in the present study with a special two-dimensional study. A soil initially at 20°C and partially-saturated with either a 0.2 or 0.5 relative liquid saturation is contained in a box two meters wide by ten meters high with impermeable bottom and sides. The upper surface of the soil is exposed to a 20°C atmosphere to which vapor and air can escape. Computation begins when the soil, which melts at 1700°C, is heated from one side (maintained at constant temperatures ranging from 1700°C to 4000°C). Heat from the hot wall causes the melt to circulate in such a way that the melt interface grows more rapidly at the top of the box than at the bottom. As the upper portion of the melt approaches the impermeable wall it creates a bottle neck for moisture release from the soil’s lower regions. The pressure history of the trapped moisture is examined as a means for predicting the potential for moisture penetration into the melt. The melt’s interface movement and moisture transport in the unmelted, porous soil are also examined.


2018 ◽  
Vol 240 ◽  
pp. 05027
Author(s):  
Mirosław Seredyński

Stabilization of the temperature of PVs is of great importance, due to strong relation between operating temperature and its efficiency. Due to low thermal conductivity of PCM, intensification of heat transfer to the operating material is needed. The four fully passive PV’s temperature stabilization systems, based on the phase change material (PCM) are numerically investigated in this paper. Apart from the natural convection promotion, intensification of heat transfer is done with aluminium fins and aluminium foam. The simplified computational model based on the equilibrium formulation of energy transport equation, taking into account viscous and inertial fluid flow resistances in the porous material, is formulated and solved with the general purpose software - ANSYS Fluent. Proposed model is succesfully verified by comparing the results with available in literature numerical solutions.Simulations outcomes are presented, the temperature and liquid fraction distributions in proposed geometry configurations, temperature variations determined in selected points and averaged on the heated surface temperature plots. Presented results help to assign the best configuration.


2013 ◽  
Vol 732-733 ◽  
pp. 297-300
Author(s):  
Ya Rong Wang ◽  
Pei Rong Wang

<strong>Heat exchanger is an equipment for general purpose. It is very popular in the industry of energy and power, refrigetion,chemical and oil. And it is also very important for company, energy and application. Its efficiency of transferring heat and its safety of operation are very important for our society, especially in these days energy becomes more and more valuable. In this paper ,we used practical examples to describe the calculation of heat transfer of surface type heat exchanger .</strong>


Author(s):  
Matjazˇ Leskovar ◽  
Bosˇtjan Koncˇar

An ex-vessel steam explosion may occur when during a severe reactor accident the reactor vessel fails and the molten core pours into the water in the reactor cavity. A steam explosion is a fuel coolant interaction process where the heat transfer from the melt to water is so intense and rapid that the timescale for heat transfer is shorter than the timescale for pressure relief. This can lead to the formation of shock waves and production of missiles at later times, during the expansion of the highly pressurized water vapor, that may endanger surrounding structures. In contrast to specialized steam explosion CFD codes, where the steam explosion is modeled on micro-scale using fundamental averaged multiphase flow conservation equations, in the presented approach the steam explosion is modeled in a simplified manner as an expanding high-pressure premixture of dispersed molten fuel, liquid water and vapor. Applying the developed steam explosion model, a comprehensive analysis of the ex-vessel steam explosion in a typical PWR reactor cavity was done using the CFD code CFX-10. At four selected locations, which are of importance for the assessment of the vulnerability of cavity structures, the pressure histories were recorded and the corresponding pressure impulses calculated. The pressure impulses determine the destructive potential of the steam explosion and represent the input for the structural mechanical analysis of the cavity structures. The simulation results show that the pressure impulses depend mainly on the steam explosion energy conversion ratio, whereas the influence of the premixture vapor volume fraction, which is a parameter in our model and determines the maximum steam explosion pressure, is not significant.


1974 ◽  
Vol 14 (06) ◽  
pp. 537-544 ◽  
Author(s):  
A.M. Garon ◽  
R.J. Wygal

Abstract The results of a systematic investigation of the parameters of fire-water flooding are reported. The parameters of fire-water flooding are reported. The results were obtained from a series of 131 combustion-tube tests. Experimental equipment and procedures were developed to minimize heat-transfer procedures were developed to minimize heat-transfer problems and transient effects at the inlet of the problems and transient effects at the inlet of the tube. The tests were performed with water/air injection ratios from 0 to 13 cu ft/Mscf, using crudes with gravities from 10 degrees to 48 degrees API, in waterflooded and nonwaterflooded sands at pressures of 0, 1,000, and 2,000 psig. The air requirements for fire-water flooding were reduced by more than 50 percent in some cases. Similar results were obtained with various crudes. Introduction The greater demand for crude oil, the increased difficulty of discovering new reservoirs, and the desire to reduce dependence on imports have emphasized the need for enhanced recovery methods capable of economically producing the crude remaining in known reservoirs. Numerous methods have been proposed and tested in laboratories and field pilots, and some have been used in commercial applications. Fire flooding is one enhanced recovery method that has been technically successful in many field applications. Some of these projects have been economically successful, but many are only marginally so. The high cost of air compression for fire flooding is one of the major factors that influence the economics. Large quantities of air are required per unit reservoir volume swept, especially for heavy crude, because all the residual material remaining in the sand immediately ahead of the combustion zone must be consumed. Only a portion of the heat generated is necessary for maintaining the movement of the combustion zone, and the remainder is left behind in the depleted sand. Fire-water flooding is a recovery technique that was conceived to improve the economics of dry fire flooding. In this process, water is injected along with the air to recover some of the heat remaining behind the combustion zone. At low water injection rates, the heat is transported through the combustion zone by superheated steam to where it can be utilized for preheating the reservoir. At higher water injection rates, the water partially quenches the combustion, reducing the maximum temperature to the steam-plateau level, and heat is transferred through the combustion zone as saturated steam. The air requirement is lower with water injection because the amount of hydrocarbonaceous material deposited on the sand grains is less and because all of this fuel is not necessarily consumed. At a constant air injection rate, the oil may be produced faster with water injection than without because of the more rapid combustion-zone movement, the increased utilization of energy, and the increased volume of fluid injected. Fire-water flooding has been investigated in several different laboratories with combustion-tube experiments. The feasibility of partially quenched combustion, the reduced air requirements, and the improved utilization of heat with water injection have been confirmed. However, the results of only a few experiments have been reported by each investigator, and only a limited amount of experimental information is available on the relationships of the fire-waterflooding parameters. in addition, it has been suggested that be results of wet combustion tests may be misleading because of experimental limitations. In this paper, the results of a systematic investigation of the parameters of fire-water flooding are reported. The results were obtained from combustion-tube tests. The equipment was designed to minimize heat-transfer problems, and operating procedures were developed that reduced the procedures were developed that reduced the transient effects at the inlet of the tube. SPEJ P. 537


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