Abstract

Introduction. In previous works, the authors proposed a new approach to the calculation of the concentration of toxic products of combustion. The approach is based on determination the volume average density of toxic gases at any given time by using their experimental dependences on the mean volume temperature. The accuracy of this approach depends heavily on the error of determining the heat losses coefficients in small-scale experimental setup and real full scale room. In this paper, using experimental data obtained on small-scale pilot plant, it is proposed a different approach, that uses the theoretical and experimental dependences between average volume densities of toxic gases and the mean volume density of oxygen. It is not necessary to determine the heat losses coefficient and also solve differential equations of the conservation laws of toxic gases masses. Materials and methods. Coniferous wood building materials, transformer oil and PVC sheath cables are considered as combustible materials. Theoretical and experimental methods of gas dynamics and heat and mass transfer are used to determine the parameters of gases mixture during free convection. Theory and calculation. A physical and mathematical model for calculating the mean volume density of carbon monoxide and toxic index for the combined effects of CO and O 2 during the combustion of solid and liquid substances and materials in conventionally hermetic volume of arbitrary sizes is proposed. The model is based on the integral method for calculating thermal and gas dynamics of fire in the room. Formulas for calculating the mean volume density of CO and toxicity index for mutual effect of the action of CO and O 2 are obtained. Results. Experimental dependencies of mean volume density of carbon monoxide and toxicity index from mean volume density of oxygen are obtained in a small-scale pilot plant. A comparison of the theoretical values of mean volume density of CO and toxicity index derived using the proposed formulas with experimental values is made. Discussion. It is shown that the volume average density of carbon monoxide and the toxicity index for the combined effects of CO and O 2 during combustion of solid and liquid materials in conventionally hermetic volume of arbitrary sizes can be calculated by using only the average volume oxygen density and specific coefficients of separation of CO and deleting O 2 . The resulting formulas for calculating the mean density of CO and toxicity index of the mutual influence of CO and O 2 do not contain the geometric sizes of the room and combustible materials surfaces and, therefore, are fair in both small-scale and large-scale fire in the room. Conclusions. The proposed physical and mathematical model allows calculation of mean volume density of CO and toxicity index for combined effects of CO and O 2 during fire in a real full-scale room without solving the differential equation of conservation law of carbon monoxide mass and using the experimental dependence between the mean volume densities of CO and O 2 and the calculated average volume density of O 2 .

Highlights

  • In previous works, the authors proposed a new approach to the calculation of the concentration of toxic products of combustion

  • The approach is based on determination the volume average density of toxic gases at any given time by using their experimental dependences on the mean volume temperature

  • In this paper, using experimental data obtained on small-scale pilot plant, it is proposed a different approach, that uses the theoretical and experimental dependences between average volume densities of toxic gases and the mean volume density of oxygen

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Summary

36 ISSN 0869-7493 ÏÎÆÀÐÎÂÇÐÛÂÎÁÅÇÎÏÀÑÍÎÑÒÜ 2017 ÒÎÌ 26 1 2

5. Çàâèñèìîñòè ñðåäíåîáúåìíîé ïëîòíîñòè îêñèäà óãëåðîäà îò èçìåíåíèÿ ñðåäíåîáúåìíîé ïëîòíîñòè êèñëîðîäà DrÎ2 ïðè ãîðåíèè îáîëî÷êè êàáåëåé ÏÂÕ, ïîëó÷åííûå ýêñïåðèìåíòàëüíî (1, 2) è ðàñ÷åòîì ïî ôîðìóëå (7) (3, 4): 1, 3 — F = 0,0067 ì2; 2, 4 — F = 0,0122 ì. 8. Çàâèñèìîñòè ïîêàçàòåëÿ òîêñè÷íîñòè Íò îò ñðåäíåîáúåìíîé ïëîòíîñòè êèñëîðîäà ïðè ãîðåíèè îáîëî÷êè êàáåëåé ÏÂÕ íà ïëîùàäè F = 0,0067 ì2 (à) è F = 0,0122 ì2 (á), ïîëó÷åííûå ýêñïåðèìåíòàëüíî (1–3) è ðàñ÷åòîì ïî ôîðìóëå (9) (4–6): 1, 4 — Hò; 2, 5 — Hò ÑÎ; 3, 6 — Hò Î2 ïîëíîìàñøòàáíîì ïîìåùåíèè áåç ðåøåíèÿ äèôôåðåíöèàëüíîãî óðàâíåíèÿ çàêîíà ñîõðàíåíèÿ ìàññû ìîíîêñèäà óãëåðîäà, à ñ èñïîëüçîâàíèåì ýêñïåðèìåíòàëüíîé çàâèñèìîñòè ïëîòíîñòè ÑÎ îò ïëîòíîñòè Î2 è ðàñ÷åòíûõ çíà÷åíèé ñðåäíåîáúåìíîé ïëîòíîñòè Î2.

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