Journal of Chemistry
Volume 2021 (2021), Article ID 6088484, 10 pages
https://doi.org/10.1155/2021/6088484

Research Article

Coupling Effect of Metals and Oxides on the Oxygen Supply Performance of Sodium Chlorate Oxygen Candle

Na Gao,1,2,3 Chunguo Ma,1,2,3 Kaeryaer Kariman,1,2,3 Jianguo Liu,1,2,3 Zheng Zhang,1,2,3 Yaqing Dai,1,2,3 and Zhao Wang1,2,3

¹School of Civil and Resource Engineering, University of Science and Technology Beijing, Beijing 100083, China
²Key Laboratory of High-Efcient Mining and Safety of Metal Mines of the Ministry of Education, University of Science and Technology Beijing, Beijing 100083, China
³Mine Emergency Technology Research Center, University of Science and Technology Beijing, Beijing 100083, China

Correspondence should be addressed to Chunguo Ma; mcg970318@163.com

Received 13 September 2021; Accepted 10 November 2021; Published 26 November 2021

Academic Editor: Josefina Pons

Copyright © 2021 Na Gao et al. This is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.

Abstract.

In this study, to explore the influence of metals and oxides on the oxygen production rate and stability of sodium chlorate oxygen candles, 28 experimental samples were investigated. The effects of Co₂O₃, Co₃O₄, and Fe₂O₃ with different mass fractions on the thermal decomposition temperature and thermal decomposition rate of sodium chlorate were compared and analyzed. Co₃O₄ (5%) was obtained to reduce the thermal decomposition range to 260–450°C and reduce the pyrolysis interval ∆T to 46.2°C. Through the development of three metals (Fe, Mg, and Mn), under four mass fractions (2%, 4%, 6%, and 8%) mixed with Co₃O₄ (5%), the results of the effective oxygen production efficiency test for the thermal decomposition reaction of sodium chlorate demonstrated that Mn (6%)–Co₃O₄ (5%) exhibited the best catalytic and heat coupling effect; the effective oxygen production efficiency of 97.8% was achieved. Oxygen candle oxygen supply experiment was conducted; the oxygen candle composition for the test was determined to be NaClO₃ (86%), Mn (6%), Co₃O₄ (5%), and kaolin (3%); in the four stages of the oxygen candle oxygen supply reaction test, the average oxygen supply rate reached 1.647 L/min, actual oxygen production was 28 L, and effective oxygen production rate of the oxygen candle was 53.6%. An increase of 9% was observed compared to the previous similar studies. The results of this study present a formula to optimize the oxygen supply of the oxygen candle, which is crucial for improving the oxygen supply performance of the oxygen candle.

1. Introduction

Oxygen candle, a solid oxygen source, possesses several advantages, such as high and fast oxygen production and large unit volume storage capacity; in addition, it has the advantages of unnecessity of additional power during use, stable usage volume, and easy to store and transport. Furthermore, the oxygen production and production rate of the oxygen candle are not affected by changes in the ambient temperature, humidity, and pressure [1–3]. Therefore, oxygen candles have been widely employed in aviation, submarine, mine rescue, and other fields [4].

Significant progress has been made in the research field of oxygen candles by various domestic and international researchers. Comparing the performance of common oxygen supply methods, Yajuan et al. analyzed the applicability of oxygen candles on plateaus [5]. Lei et al. analyzed the feasibility of the application of oxygen candles in deep-sea manned submersibles and proposed technical indicators suitable for emergency oxygen supply in deep-sea manned submersibles [6]. Shu et al. conducted a series of simulation tests and discussed the impact of oxygen candles on the living environment of a mining hazard space [7]. Shafirovich et al. used differential thermal analysis (DTA)/thermogravimetric analyzer (TGA) combined thermogravimetric analysis to conduct a binary thermogravimetric analysis of five common metals—Al, Fe, Co, Ni, and Sn—and NaClO₃; they investigated the catalytic effects of five metals on the thermal decomposition of NaClO₃ [8]. Gao and Liu [9, 10] optimized the oxygen production technology of the chlorate oxygen candle; in particular, they optimized the working principle, raw materials, and starting method [9] and studied the influence of manganese metal fuel on the pyrolysis of sodium chlorate oxygen candle [10].

The existing research results in this field are mainly to analyze the influence of single factor on the catalytic effect and technical index of oxygen candle. The coupling effect of metal and oxide on the oxygen supply performance of oxygen candles and the oxygen supply efficiency in closed space are lacking. Based on the previous research results and the oxygen production mechanism of NaClO₃ pyrolysis, the effects of oxides (Co₂O₃, Co₃O₄, and Fe₂O₃) and metals (Fe, Mg, and Mn) on the pyrolysis of NaClO₃ were compared and analyzed by thermogravimetric experiment. An optimized formula of oxygen candle with higher efficiency and better catalytic performance than the previous research was proposed, and the application effect of oxygen candle oxygen supply was verified by the oxygen candle oxygen supply test. The research conclusions provide a reference for improving the multifactor coupling oxygen supply performance of sodium chlorate oxygen candle.

2. Materials

2.1. Test Reagents and Instruments

2.1.1. Test Reagents

NaClO₃, analytically pure, Fe, Mg, and Mn were purchased from Beijing Tongguang Fine Chemical Co., Ltd. Co₂O₃ (99.9%), Co₃O₄ (99.9%), Fe₂O₃ (99.9%), and kaolin were purchased from Beijing Yihua Chengda Technology Co., Ltd. Silica aerogel felt insulation material was purchased from Zhongwei (Tianjin) Technology Co., Ltd.

2.1.2. Test Instruments

The test instruments include the constant temperature drying oven (DHG-9070A, Shanghai Jinghong Experimental Equipment Co., Ltd.), omni-directional planetary ball mill (QM-QX10, Nanjing University Instrument Factory), pressure testing machine (YES-300, Jinan Huaxing Experimental Equipment Co., Ltd.), thermal heavy mass spectrometer (STA449F3A-0660-M, Netzsch, Germany), and multifunction gas detector (Anpal Technology Co., Ltd.).

2.2. Experimental Methods

2.2.1. Sample Preparation

Thermal Decomposition Reaction. To avoid the influence of free water vapor in the medicine on the test, NaClO₃ was placed in a constant temperature drying oven at 80°C for 8 h before sample preparation; the sample proportioning was performed according to Table 1. We added 10 g of the proportioned sample to the ceramic crucible and manually stirred it for 10 min. A total of 28 samples were prepared.

Table 1: Proportioning table for the thermogravimetric experiment.

Sample
NaClO₃
Co₂O₃
Co₃O₄
Mass fraction (%)
Significance

Fe₂O₃
Fe
Mg
Mn

1#
100
0
0
0
0
0
0
Blank test

2#
98
2
0
0

Analyze the influence of oxides on the thermal decomposition temperature range and rate of sodium chlorate

3#

0
2
0

4#

0
0
2

5#
97
3
0
0

6#

0
3
0

7#

0
0
3

8#
96
4
0
0

9#

0
4
4

10#

0
0
0

11#
95
5
0
0

12#

0
5
0

13#

0
0
5

14#
94
6
0
0

15#

0
6
0

16#

0
0
6

17#
93
0
5
0
2
0
0
Analyze the effect of mixing metal and Co₃O₄ (5%) on the effective oxygen production efficiency of sodium chlorate thermal decomposition

18#

0
2
0

19#

0
0
2

20#
91

4
0
0

21#

0
4
0

22#

0
0
4

23#
89

6
0
0

24#

0
6
0

25#

0
0
6

26#
87

8
0
0

27#

0
8
0

28#

0
0
8

Oxygen Candle Oxygen Supply Reaction. Based on the previous research results, the oxygen candle composition for the test was determined to be NaClO₃ (86%), Mn (6%), Co₃O₄ (5%), and kaolin (3%). The oxygen candle structure adopts a hollow structure, which promotes the reaction [11]. The composition, mass (Table 2), and size (inner diameter: 10 mm, outer diameter: 60 mm, and height: 64.5 mm) of the oxygen candle for the test can be calculated according to equations (1) and (2).

Table 2: Quality of the sample required for the experiment.

Materials
NaClO₃
Mn
Co₃O₄
Kaolin
Total

Weight (g)
274.2
18.7
15.6
9.5
318

Theoretical Oxygen Supply of Oxygen Candle for Test. The absolute value of the maximum oxygen uptake of healthy adult men in China is 3.0 L/min–3.5 L/min; we assumed the uptake value as 3.5 L/min to prepare a sufficient amount of oxygen. Considering the influence of the volume of the oxygen candle during the oxygen supply test, to meet the 15 min oxygen demand of a healthy adult male, we determined an appropriate size for the oxygen candle during preparation. The oxygen demand calculation is as follows.

where V15min is the 15 min oxygen demand of healthy adult men, Vn is the absolute value of the maximum oxygen uptake, and t is the maximum oxygen uptake time.

Composition and Quality of Oxygen Candle for Test. According to the main reaction equation of the oxygen candle production, the mass of the oxygen candle sample required to produce 52.5 L of oxygen was calculated, as given in Table 2.

Oxygen Candle Volume Size for Test. The density of the oxygen candle compressed by the oxygen candle selected in this test was in the range of 1.8 g/cm³–2.0 g/cm³, and the quality of the medicine required for the test was 318 g. According to equation (2), the volume of the oxygen candle required for an adult to breathe for 15 minutes was 176.7 cm³, inner diameter of the oxygen candle was 10 mm, outer diameter was 60 mm, and height was 64.5 mm.

where, VOxygen is the volume of the oxygen candle sample, m is the mass of the oxygen candle sample, and is the density of the oxygen candle sample.

We used an omni-directional planetary ball mill to grind and mix the sample for 5 min at a speed of 280 rpm and placed the ground oxygen candle sample into a self-made compression mold as shown in Figure 1. Subsequently, we used a pressure testing machine to pressurize the sample with a force of 35 KN. The oxygen candle body for the test was obtained from the mold [12], as shown in Figure 2.

Figure 1: Pressing mold of hollow structure oxygen candle.

Figure 2: Oxygen candle test sample.

2.2.2. Thermal Decomposition Reaction Test

We used Netzsch STA449F3A-0660-M thermogravimetric-mass spectrometry combined analysis equipment to perform thermal decomposition reaction tests on 28 samples. Herein, 15 ± 2 mg of each group of samples was weighed each time and placed in the thermogravimetric analyzer; subsequently, thermogravimetric analysis was conducted. The starting temperature of the test was 25 ± 3°C, target temperature was 750°C, heating rate was 20°C/min, test gas was Ar, and flow rate was 40 mL/min.

2.2.3. Oxygen Candle Reaction Experiment

Based on the previous research conclusions, the oxygen candle sample (86% NaClO₃, 6% Mn, 5% Co₃O₄, and 3% kaolin) used in this experiment had an inner diameter of 10 mm, an outer diameter of 60 mm, and a height of 64.5 mm. The weight of a single sample was 318 g. The oxygen candle sample was placed in the reaction device, and silica aerogel felt was placed in the heat insulation structure as the heat insulation material; subsequently, this assembly was connected to the test instrument. The oxygen candle was placed in a closed box with a volume of 216 L, the remote ignition method was used to ignite it, and the Anpal multifunctional gas detector was used to monitor the gas concentration and oxygen production rate changes during the oxygen supply process of the oxygen candle. The gas detector data transmission module was used to output and analyze the experimental data as shown in Figure 3.

Figure 3: Connection diagram of the oxygen candle oxygen test equipment.

3. Results and Discussion

3.1. NaClO₃ Pyrolysis Reaction Analysis

The combined thermogravimetric experiment and 1# sample were used to analyze the thermal decomposition reaction process of pure NaClO₃; the thermogravimetric (TG) curve obtained is shown in Figure 4 as a blank test. Pure NaClO₃ began to decompose at approximately 520°C, TG curve began to decrease, and thermal decomposition reaction ended at approximately 600°C. The TG curve obtained was smooth, indicating that the pyrolysis process of pure NaClO₃ is relatively stable. The main reaction equation is shown in the following equation [13, 14]. By comparing the process and regular pattern of the thermal decomposition reaction between the test sample and pure NaClO₃, the effect of the catalyst and metal on the thermal decomposition reaction of NaClO₃ was determined.

Figure 4: TG curve of thermal decomposition reaction of NaClO₃.

The oxychloride anode comprises sodium oxychloride, metal fuel, oxide catalyst, and binder. Past research evidence shows that oxides can be catalysts, and the characteristic properties of metal oxide reactions form thermal reactions to provide energy. This study analyzed the effects of three oxides (Co₂O₃, Co₃O₄, and Fe₂O₃) and three metals (Fe, Mg, and Mn) on the thermal decomposition of NaClO₃ [15].

3.2. Analysis of the Influence of Oxide on the Thermal Decomposition Reaction of NaClO₃

3.2.1. Analysis of the Influence of Oxide on the Thermal Decomposition Temperature of NaClO₃

According to the ICTAC regulations [12], the pyrolysis rate (TG) in the thermogravimetric test can be calculated by equation (4).

where mt is the mass of the sample at time t, m₀ is the mass of the sample at the beginning of pyrolysis.

Three oxides of Co₂O₃, Co₃O₄, and Fe₂O₃ were selected as catalysts, and the mass fractions of each oxide were 2%, 3%, 4%, 5%, and 6%, and the 15 samples above are used to carry out the NaClO₃ thermal decomposition reaction test. The thermogravimetric curve of each sample is shown in Figure 5. After adding the oxides (Co₂O₃, Co₃O₄, and Fe₂O₃) to NaClO₃, the temperature ranges for the initiation and termination of the thermal decomposition reaction were 348–552°C (Co₂O₃), 260–450°C (Co₃O₄), and 366–558°C (Fe₂O₃), respectively. For the same oxide, the temperature and range of the starting and ending reaction of the thermal decomposition reaction decreased with the increase in the oxide content. Among them, the oxide mass fractions of 5% and 6% did not significantly effect on the temperature and range of the thermal decomposition reaction. The order of the lowering effect of the three oxide catalysts on the pyrolysis temperature of NaClO₃ is Co₃O₄ > Co₂O₃ > Fe₂O₃. Therefore, Co₃O₄ is the best catalyst to control the temperature range of the thermal decomposition reaction.

(a)

(b)

(c)

Figure 5: NaClO₃ oxide TG curve. (a) NaClO₃–Co₂O₃ TG curve. (b) NaClO₃–Co₃O₄ TG curve. (c) NaClO₃–Fe2O₃ TG curve.

3.2.2. Analysis of the Influence of Oxides on the Thermal Decomposition Rate of NaClO₃

The conversion rate (α) in the thermogravimetric test can be calculated by the following equation.

where m₀ is the mass of the sample at the beginning of pyrolysis, mt is the mass of the sample at time t, and mf is the mass of the sample at the end of pyrolysis.

In this study, the temperature pyrolysis characteristic temperature corresponding to the conversion rates α = 0.1 and α = 0.9 was recorded as T0.1 and T0.9, i.e., pyrolysis starting temperature and ending temperature, respectively. The characteristic temperature is shown in Figure 6. The difference between the two is regarded as the pyrolysis interval (∆T = T0.9 − T0.1). At a constant heating rate of 20°C/min, the smaller the ∆T, the shorter the pyrolysis time of the sample, and the faster the pyrolysis rate and vice versa.

(a)

(b)

(c)

Figure 6: NaClO₃ oxide pyrolysis characteristic temperature curve. (a) NaClO₃–Co₂O₃ pyrolysis characteristic temperature curve. (b) NaClO₃–Co₃O₄ pyrolysis characteristic temperature curve. (c) NaClO₃–Fe₂O₃ pyrolysis characteristic temperature curve.

It can be seen from Figure 6 that the initial reaction temperature T0.1 of NaClO₃ decreases with the increase of the oxide mass fraction. Among the three oxides, T0.1min was 260°C (Co₃O₄-6%) and T0.1max was (Fe₂O₃-2%). The NaClO₃ termination reaction temperature T0.9 decreased with the increase of the oxide mass fraction. T0.9min was 306°C (Co₃O₄, 6%), and T0.9max was 559°C (Fe₂O₃, 2%). For the same oxide, as the mass fraction increased, T0.1 and T0.9 gradually decreased; however, when the mass fraction was between 4% and 6%, the effect on T0.1 and T0.9 was small, that is, the catalytic effect change was relatively low.

By analyzing the influence of oxides on T0.1 and T0.9, it was observed that ∆T increases with the increase of the mass fraction of Co₂O₃, decreases with the increase of the Co₃O₄ content, and decreases with the increase of the mass fraction of Fe₂O₃. The smaller the ∆T, the faster the pyrolysis rate. Therefore, among the three metal oxides, Co₃O₄ (5-6%) corresponded to the smallest ∆T, which was 46.2°C, which is 14°C lower than that of pure NaClO₃. Consequently, Co₃O₄ has the best effect on accelerating the decomposition rate of NaClO₃ thermal decomposition reaction.

3.2.3. Determination of High-Efficiency Oxide Catalyst Components

According to the analysis of the influence of oxides on the thermal decomposition reaction, it can be seen that among the three oxide catalysts, Co₃O₄ (5-6%) reduces the temperature range of the initiation and termination of the thermal decomposition reaction and has the best effect on accelerating the rate of thermal decomposition reaction. The corresponding T0.1 was 260°C, T0.9 was 306.2°C, and ∆T was 46.2°C; the catalytic effect did not change significantly within this range. Therefore, to increase the weight of NaClO₃ in the thermal decomposition reaction mixture and ensure more oxygen generation, the Co₃O₄ (5%) was selected in this study.

3.3. Analyzing the Coupling Effect of Metal Oxide on Effective Oxygen Production Rate

Based on the previously reported studies [9–13], we selected four different proportions (2%, 4%, 6%, and 8%) of three metals (Fe, Mg, and Mn) mixed with Co₃O₄ (5%) and analyzed the metal oxide effect on the thermal decomposition reaction of NaClO₃. The effective oxygen production efficiency of 17–28# (a total of 12) samples can be calculated as follows:

where NO2 is the effective oxygen production efficiency, QAO2 is the actual oxygen production, QTO2 is the theoretical oxygen production, TG is the weight loss ratio of the sample, m₀ is the initial mass of the sample, VO2 is the volume of 1 mol O₂ under standard conditions, which is 2.24 × 10⁴ mL, mO2 is the mass of 1 mol of O₂ under the standard condition, which is 3.2 × 10⁴ mg, NaClO₃ is the mass fraction of NaClO₃ in the sample, and mNaClO3 is the mass of 1 mol of NaClO₃ under the standard condition, which is 1.061 × 105 mg.

Figure 7 shows that when single metal (2%, 4%, 6%, and 8%) is added, the corresponding effective oxygen production efficiency (NO2) of Fe (4%), Mg (8%), and Mn (6%) is higher, which is 96.5%, 97.2%, and 97.8%, respectively. For the same metal mass fraction, NO2 of 2% (Mn), 4% (Fe), 6% (Mn), and 8% (Mg) is higher, which is 95.1%, 96.5%, 97.8%, and 97.2%, respectively. Among these, NO2 of Mg (6%)–Co₃O₄ (5%) is the highest, which is 97.8%. Therefore, Mn (6%)–Co₃O₄ (5%) was selected as the metal fuel and catalyst of the oxygen candle body.

Figure 7: NaClO₃–5% Co₃O₄ metal effective oxygen production efficiency curve.

3.4. Experimental Analysis of the Oxygen Supply Reaction of Oxygen Candle

The oxygen supply reaction experiment can obtain the oxygen candle O₂ production rate curve (Figure 8) and the oxygen candle O₂ concentration curve (Figure 9). The experiment was carried out for 53 min, and the entire oxygen supply reaction was divided into four stages: the initial reaction stage (0–6 min), rapid rise stage (6–13 min), rapid decline stage (13–17 min), and stable end-stage (17–53 min). In the initial reaction stage, the oxygen production rate in the reaction space was 0 L/min, and the oxygen concentration was maintained at 20%. This shows that the oxygen candle reacted slowly in the initial stage, and the gas monitoring system did not detect the generation of oxygen, and thus, the oxygen concentration in the reaction space did not change significantly. In the rapid rise stage, the oxygen production rate in the experimental space increased rapidly from 0 to 17.28 L/min, and the oxygen concentration reached the peak value of 50%, indicating that the rapid reaction at this stage resulted in a large amount of oxygen, and the gas monitoring system detected a large amount of oxygen around the oxygen candle. During the rapid decline stage, the oxygen production rate in the experimental space decreased rapidly from 17.28 to 0.5 L/min, and the oxygen concentration decreased to 33%. This shows that the oxygen supply reaction at this stage entered a slow stage, and the gas generated in the rapid ascent stage is gradually and evenly distributed in the test space; in addition, the oxygen concentration monitored by the gas monitoring system decreases gradually. At the stable end-stage, the oxygen production rate in the experimental space gradually tended to 0 L/min, and the oxygen concentration was maintained at 33%. This shows that the oxygen supply reaction of the oxygen candle at this stage is over, and the gas monitoring system shows that the space oxygen vacancy remains unchanged.

Figure 8: Oxygen candle O₂ production rate curve of test space.

Figure 9: Oxygen candle O₂ concentration curve of test space.

According to the following equations, the actual oxygen production of the oxygen candle oxygen supply device was 28 L, and the effective oxygen production rate was 53.6%.

where NE is the effective oxygen production rate of the oxygen candle, VA is the actual oxygen production of the oxygen candle, VT is the theoretical oxygen production of the oxygen candle, which is 52.2 L, Cs is the oxygen concentration in the test space during the stable phase of the oxygen supply reaction of the oxygen candle, Ci is the oxygen concentration in the test space at the initial stage of the candle oxygen supply reaction, and Vb is the test space volume.

According to the following equation, the average oxygen production rate during the oxygen candle oxygen experiment was 1.647 L/min.

where is the average oxygen production rate in the oxygen candle oxygen experiment, and TA is the reaction time of the oxygen candle in the oxygen candle oxygen experiment, which is 17 min.

4. Conclusion

(1)When the oxide catalysts (Co₂O₃, Co₃O₄, and Fe₂O₃) were added separately, the pyrolysis temperature of NaClO₃ reduced significantly, which decreased gradually with an increase in the mass fraction of the catalyst. When the mass fraction of the catalyst reached 4–6%, the pyrolysis temperature of NaClO₃ remains unchanged. The thermal decomposition temperature remained unchanged. The lowering effect of the three different oxides on the pyrolysis temperature of NaClO₃ was in the following order: Co₃O₄ > Co₂O₃ > Fe₂O₃. The order of pyrolysis rate was Co₃O₄ > Co₂O₃ > Fe₂O₃, and finally, Co₃O₄ (5%) was selected as the catalytic high-efficiency agent.(2)When 2%, 4%, 6%, and 8% of metal (Fe, Mg, and Mn)-Co₃O₄ (5%) were added, the order of the effective oxygen production efficiency of Fe metal for NaClO₃ is Fe (4%) > Fe (6%) > Fe (2%) > Fe (8%), the order of the effective oxygen production efficiency of Mg metal for NaClO₃ is Mg (8%) ＞ Mg (4%) ＞ Mg (6%) ＞ Mg (2%), the order of the effective oxygen production efficiency of Mn metal for NaClO₃ is Mn (6%) ＞ Mn (8%) ＞ Mn (4%) ＞ Mn (2%), and the order of the effective oxygen production efficiency of different metals for NaClO₃ is Mn (6%) > Mg (8%) > Fe (4%). Finally, Mn (6%)-Co₃O₄ (5%) was selected as the metal fuel and catalyst of the oxygen candle body, with the highest oxygen production efficiency of 97.8%.(3)Oxygen candle oxygen supply experiment showed that the optimized oxygen candle prescription (86% of NaClO₃, 6% of Mn, 5% of Co₃O₄, and 3% of kaolin) oxygen supply reaction is divided into four stages: initial reaction stage (0–6 min), rapid rise stage (6–13 min), rapid decline stage (13–17 min), and stable end-stage (17–53 min). The actual oxygen production was 28 L, average oxygen production rate was 1.647 L/min, and the effective oxygen production rate of the oxygen candle was 53.6%, which confirm an increase of 9% compared to that reported previously.(4)Although the optimal ratio of oxygen candle and its actual oxygen supply efficiency are obtained through experiments, the specific equipment for oxygen supply by oxygen candle is not studied. In the future research, the basic theoretical research of oxygen supply by oxygen candle should be combined with the practical application equipment to realize the transformation of achievements.

Data Availability

The data used to support the findings of this study are available from the corresponding author upon request.

Conflicts of Interest

The authors declare that they have no conflicts of interest.

Acknowledgments

This work was supported by the National Natural Science Foundation of China (51504017) and the funds for basic scientific research operations of Central Universities in China (FRF-RDRY-20-028).

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