Qu
Liang‡
a,
Pingxiao
Liu‡
d,
Lei
Zhao
*c,
Xuejun
Wang
c,
Jun
Zou
c,
Xun
Bao
a,
Qiangling
Zhang
a,
Wei
Xu
a,
Xue
Zou
a,
Shifeng
Wang
*d,
Chaoqun
Huang
a,
Chengyin
Shen
*ab and
Yannan
Chu
ab
aAnhui Province Key Laboratory of Medical Physics and Technology, Institute of Health and Medical Technology, Hefei Institutes of Physical Science, Chinese Academy of Sciences, Hefei, 230031, P.R. China. E-mail: chyshen@aiofm.ac.cn
bHefei Cancer Hospital, Chinese Academy of Sciences, Hefei, 230031, P.R. China
cNo. 719 Research Institute, China State Shipbuilding Corporation, 430200, Wuhan, P.R. China
dNaval Medical Research Institute, Shanghai, 200433, P.R. China
First published on 6th May 2025
The multiple gas mixtures in the deck decompression chamber (DDC) serve as a life-sustaining medium for divers to adapt to high-pressure environments and to safely decompress after saturation diving operations. However, due to the complexity of the gas composition and the wide concentration range, there is currently no technique that can rapidly detect all gases in the DDC. In this study, we developed a photoinduced chemical ionization (pCI) and electron impact (EI) dynamic switching mass spectrometry system. This technique was applied to investigate the spatial distribution uniformity of respiratory gases within the DDC at pressures of 0.13 MPa, 0.6 MPa, and 1.5 MPa, as well as the removal efficiency of toxic gases at 1.5 MPa. The switching stability time of pCI/EI dynamic switching mass spectrometry was 30 s per cycle, with optimal detection performance metrics including a detection limit down to 0.58 ppb (H2S), a fastest response time of 2 s (for CO2 and H2S), sensitivity up to 62.97 counts per ppb (H2S), and an overall concentration detection range spanning from 1.0 × 10−9 v/v (1 ppb) to 4.5 × 10−1 v/v (45%), covering the requirements for all target gases. At the three pressure levels, the spatial distribution uniformity of O2 in the DDC was 0.34%, 0.21%, and 0.08%, with the time to reach uniform distribution being 5 min, 3 min, and 1 min, respectively. For CO2, the spatial distribution uniformity was 0.62%, 1.61%, and 1.30%, with uniform distribution achieved in 10 min, 7 min, and 5 min, respectively. The removal efficiencies for harmful gases such as CO2, CH4, NH3, and H2S were 39.57%, 10.75%, 14.29%, and 3.96%, respectively. Under high-pressure conditions, O2 and CO2 rapidly achieved uniform distribution within the DDC. The pCI/EI dynamic switching mass spectrometry technology provides a rapid detection method for multicomponent gases in enclosed chambers like the DDC. This technology holds significant implications for the life support and operational efficiency of personnel involved in shipwreck salvage, underwater construction, and deep-sea exploration of marine resources.
Currently, the techniques used to detect multiple gas mixtures within the DDC include sensor technology, spectroscopy, and mass spectrometry. Sensor technology is suited for detecting specific types of gases. Lillo et al. integrated sensors for NH3, carbon monoxide, chlorine, hydrogen chloride, hydrogen cyanide, H2S, nitrogen dioxide, and sulfur dioxide gases to achieve real-time online detection of gases at ppm levels in high-pressure chambers.12 Although combining multiple sensors can enable real-time online detection of multicomponent gases in the DDC, sensor technology has limited detection capabilities for trace gases such as NH3 and H2S. Spectroscopy, on the other hand, enables qualitative and quantitative analysis of gases by measuring the absorption of specific light frequencies by gas molecules. Lillo et al. developed an in situ online CO2 monitor for high-pressure environments, enabling real-time monitoring of CO2 in a dry deck shelter at six absolute atmospheres.13 However, since different gases require lasers of different frequencies, single-frequency spectroscopy cannot simultaneously detect multiple gas mixtures. While both sensor and spectroscopy technologies can operate directly under high-pressure conditions and enable rapid in situ detection of gases in the DDC, neither can simultaneously detect all multiple gas mixtures within the chamber.
Mass spectrometry, including gas chromatography–mass spectrometry (GC-MS), is a commonly used technique for qualitative and quantitative analysis of gas mixtures.14 GC-MS requires offline sampling, followed by the selection of appropriate chromatographic columns and sample pretreatment methods (e.g., dilution or concentration) based on the polarity and concentration of the gases,15,16 making the analysis process complex and time-consuming. Online mass spectrometry techniques, such as electron impact mass spectrometry (EI-MS), have been employed for gas detection in enclosed chambers. Arieli et al. directly inserted a high-resistance sampling capillary into a high-pressure chamber with pressures ranging from 0.10 MPa to 0.51 MPa and utilized EI-MS to conduct real-time online monitoring of high concentrations of O2 (up to 21%) and CO2 (up to 5%) within the chamber.17 To protect the health of astronauts aboard space stations, EI-MS has also been used for the direct monitoring of permanent gases such as O2, N2, CO2, and CH4 in the space station environment.14,18 Although the 70 eV electrons in EI-MS can ionize most gases,19 interactions between electrons and gas mixtures often result in competition between high-concentration matrix gases like O2 and CO2 and trace gases such as H2S and NH3, limiting the ionization efficiency of trace gases.20 In contrast, photoinduced chemical ionization mass spectrometry (pCI-MS) enables rapid and highly sensitive detection of H2S and NH3.21,22 However, due to the high sensitivity of pCI-MS, it is generally used to detect ppbv or even lower concentration gases, which is not suitable for detecting high concentration gases such as O2, CO2, and CH4 in DDC.
In this study, we aim to develop pCI and EI dynamic switching mass spectrometry capable of simultaneously detecting multiple gas mixtures within the DDC. First, the structure of the dual-source dynamic switching mass spectrometry system and dynamic switching mode will be introduced. Next, the instrument's performance will be evaluated. Finally, dual-source dynamic-switching mass spectrometry will be utilized to examine the uniformity of gas distribution under various operating conditions (0.13 MPa, 0.5 MPa, and 1.5 MPa) in an unmanned deck decompression chamber, as well as the removal efficiency of harmful gases at 1.5 MPa. This instrument offers a rapid and precise method for detecting multiple gas mixtures in the DDC and provides a refined tool for detecting the quality of breathing gas for divers engaged in saturation diving.
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Fig. 1 The structure of the DDC and the process for sampling and analyzing the multiple gas mixtures. |
The pCI source comprises a photoionization Kr lamp and a radio frequency (RF) ion funnel drift tube. The Kr lamp emits photons with an energy of 10.60 eV.23 The RF ion funnel drift tube is composed of stainless steel ring electrodes with a linearly varying inner diameter, sealed with polytetrafluoroethylene gaskets. The stainless steel electrodes are subjected to both RF and direct current (DC) voltages. During the operation of the pCI source, the frequency of the RF is set to 1 MHz, the amplitude of the RF voltage is 100 V, and the DC electric field strength within the reaction tube is 4.62 V cm−1.
The ionization energies of H2S and NH3 are 10.46 eV and 10.07 eV, respectively, both of which are lower than the 10.60 eV energy of the Kr lamp. Therefore, both compounds can undergo single-photon ionization, resulting in the formation of molecular ion peaks (M+) and the release of electrons. The ionization process is as follows:
H2S + hv → H2S+ + e− | (1) |
NH3 + hv → NH3+ + e− | (2) |
In our experimental system, a large amount of H3O+ ions was observed, which may originate from the reaction of electrons (e−) released during the photoionization process with residual water molecules, though the specific mechanism requires further investigation. The ionization process produces prominent H3O+ ions (m/z 19), which subsequently undergo proton transfer reactions with H2S/NH3 to form H3S+ (m/z 35) and NH4+ (m/z 18), as shown by the characteristic peaks in Fig. S1.†
When the EI source is in operation, the RF ion funnel drift tube does not apply RF or DC voltages. CH4, O2, and CO2 pass directly through the drift tube into the mass spectrometry chamber. In the mass spectrometry chamber, the EI source generates electrons with an energy of 70 eV. These electrons collide with CH4, O2, and CO2, producing molecular ion peaks and fragment peaks. During the operation of either the pCI or the EI source, the temperature of the drift tube is maintained at 80 °C, and the pressure within the reaction tube is maintained at 0.8 hPa. The sample introduction line consists of passivized stainless steel capillaries, with a sample flow rate of 48 mL min−1. The quadrupole mass analyzer has a mass analysis range of 0.1 amu to 510 amu and operates at a pressure of 3.2 × 10−6 hPa (the pressure remains constant during ion source switching). The electrical control system manages the dynamic switching of the pCI and EI sources and the corresponding mass spectrometry parameters, as well as data acquisition. The switching process is automatically completed by the control system based on the set parameters. Additionally, to demonstrate the characteristics of the dual ion source system, as shown in the ESI Fig. S2,† we compared the performance of pCI-MS and EI-MS when detecting typical target compounds. The pCI mode exhibits higher selectivity and sensitivity for H2S and NH3 and can effectively suppress background gas interference. In contrast, the EI mode is suitable for detecting inorganic gases like N2.
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Fig. 3 The signal response changes of (a) CH4, (b) CO, (c) O2, (d) H2S and (e) NH3 during ionization source switching under actual working conditions. |
As illustrated in Fig. 3(a)–(c), when switching from pCI-MS to EI-MS, the ionic signals of CH4, CO2, and O2 require approximately 30 seconds (t1) to achieve stability. During the initial activation of the EI source, significant signal oscillations are observed (potentially associated with electron emission stabilization and plasma formation processes), with signals beginning to approach a steady state at approximately t1/2.
In contrast, as demonstrated in Fig. 3(d) and (e), the reverse transition (EI → pCI) exhibits a markedly reduced stabilization time of less than 1 second (t2) for NH3 and H2S ionic signals. This temporal disparity primarily stems from the distinct physical mechanisms governing the two switching processes: t1 (pCI → EI) encompasses both the physical transition time of the ion source and the period required for the EI source to establish electron emission equilibrium and stabilize plasma conditions, whereas t2 (EI → pCI) predominantly involves the deactivation of the EI source and the instantaneous initiation of the Kr lamp, which rapidly establishes a stable photoionization state.
These findings validate the practical utility of the dual ion source system in real-world applications: although the transition from pCI mode to EI mode necessitates a certain preheating period, the system can promptly resume analytical capabilities upon returning from EI mode to pCI mode, rendering it suitable for analytical requirements demanding flexible alternation between the two modes. Additionally, these observations provide valuable reference for experimental protocol design—the extended preheating time of EI-MS may require consideration in time-sensitive applications.
The use of the pCI source enabled efficient soft ionization of trace gases such as NH3 and H2S, while most matrix gases (e.g., N2, O2, and CO2) could not be detected due to their inability to undergo proton transfer reactions. In contrast, when ionizing trace gases, the EI source exhibited limited ionization efficiency, making it difficult for mass spectrometry to detect these trace gases. However, the EI source produced clear signals for high-concentration matrix gases such as N2, O2, and CO2. By flexibly combining and switching between the EI and pCI sources, rapid detection of a wide range of gas concentrations was achieved without the need to replace hardware. This approach saved significant time and improved experimental efficiency. However, the rapid switching between the dual sources imposes higher demands on the reliability of key components.
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Fig. 4 (a) Standard curve of O2 in EI-MS mode; (b) standard curves of CH4 and CO2 in EI-MS mode; (c) the standard curve of NH3 in pCI-MS mode; (d) standard curve of H2S in pCI-MS mode. |
m/z | Response times (s) | LODs | GB-18435-2007 (China) | |||
---|---|---|---|---|---|---|
1 | EI-MS | CH4 | 16 | 4 | 210.60 ppm | 872.46 ppm |
2 | O2 | 32 | 4 | 841.90 ppm | — | |
3 | CO2 | 44 | 2 | 20.13 ppm | 33.67 ppm | |
4 | pCI-MS | NH3 | 18 | 11 | 0.13 ppm | 0.68 ppm |
5 | H2S | 35 | 2 | 0.58 ppb | 4.83 ppb |
During the gas equilibrium test, the ambient temperature remained stable at approximately 23 °C, and the relative humidity inside the DDC ranged from 50% to 60%. The pressure control device was operated to pressurize the DDC with synthetic air (before reaching the target pressure). High-purity O2 and CO2 were then introduced into the DDC simultaneously from high-pressure O2 and CO2 cylinders (until the DDC pressure reached the target value). Three pressure conditions were tested in the DDC: 0.13 MPa, 0.6 MPa, and 1.5 MPa. Under each condition, 500 L of O2 and 80 L of CO2 (at 23 °C and 0.1 MPa) were introduced. The gas equilibrium system was activated, and from time zero, air samples were collected at regular intervals from seven spatial sampling points in the DDC. For each point, five gas samples were collected using sampling bags, and the samples were analyzed using the pCI/EI-MS. The test primarily evaluated the spatial distribution uniformity of O2 and CO2. During the mass spectrometric analysis of the samples, only the EI source was used, with a dwell time of 1 s.
At a pressure of 0.13 MPa, the concentration changes of O2 and CO2 inside the DDC are shown in Fig. 5(a and d). At 0.13 MPa, the time required for O2 to reach spatial equilibrium was 5 minutes. During this process, the average O2 concentration across the seven spatial sampling points exhibited a linear increase, and the relative standard deviation (RSD) of the concentration distribution among the seven sampling points was 0.49%. After 5 minutes, the concentrations at all seven sampling points reached equilibrium, with an RSD of 0.23%, indicating a 56.36% reduction in spatial fluctuation. This result suggests that the seven sampling points were not spatially equivalent, leading to differences in O2 concentrations during equilibrium. These differences were likely due to the varying distances of the sampling points from the gas equilibrium device. For CO2, the time to reach spatial equilibrium at 0.13 MPa was 10 minutes. The CO2 concentrations in the seven spatial sampling bags also exhibited a linear increase, and as shown in Fig. 5(d), the concentrations at sampling points S7, S5, and S1 were noticeably higher than those at S2, S3, S4, and S6 during equilibrium, further indicating spatial variation among the sampling points. The equilibrium time for CO2 was twice that of O2 at 0.13 MPa. Despite having the same average molecular kinetic energy at the same temperature, O2 has a lower molecular weight than CO2, resulting in faster diffusion of O2. Furthermore, when comparing the relative concentration increases before and after equilibrium, O2 exhibited a 14.81% increase, while CO2 showed a 178.66% increase. Considering the diffusion speed and concentration differences before and after equilibrium, O2 reached equilibrium faster with a smaller increase in concentration, resulting in a shorter spatial equilibrium time. The RSD of CO2 spatial fluctuation before equilibrium was 6.33%, while after equilibrium, it was 2.52%, representing a 60.19% reduction. This outcome was also due to the varying distances of the sampling points from the gas equilibrium device.
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Fig. 5 The concentration change of O2 (a–c) and CO2 (d–f) at seven spatial sampling points with time under 0.13 MPa, 0.6 MPa and 1.5 MPa pressure in DDC. |
At a pressure of 0.6 MPa, the changes in O2 and CO2 concentrations within the DDC are shown in Fig. 5(b and e). Compared to the spatial equilibrium time of 5 minutes at 0.13 MPa, the time for O2 to reach equilibrium in the DDC decreased to 3 minutes at 0.6 MPa. At 1.5 MPa, the equilibrium time further reduced to 1 minute, as shown in Fig. 5(c). This reduction in equilibrium time is related to the increased diffusion rate of O2 and the smaller concentration increase before and after equilibrium. At constant temperature, the average kinetic energy of O2 remains unchanged, but with increasing pressure, the frequency of O2 collisions with surrounding molecules increases, leading to a faster diffusion rate in the DDC. Additionally, the concentration increments of O2 at 0.6 MPa and 1.5 MPa were 1.47% and 1.19%, respectively, further contributing to the reduced equilibrium time. The spatial equilibrium time for CO2 was approximately 7 minutes at 0.6 MPa and decreased to 5 minutes at 1.5 MPa. As the pressure in the DDC increased, the spatial equilibrium times for both O2 and CO2 shortened.
As shown in Fig. 5(a–c), the spatial equilibrium times for O2 in the DDC were 5 minutes, 3 minutes, and 1 minute, respectively. After equilibrium, the O2 concentrations were 23.16% (±0.34%), 20.47% (±0.21%), and 20.04% (±0.08%). The results indicate that the distribution deviations of O2 in the DDC under different conditions were consistent, with the RSD values not exceeding 0.34%, demonstrating good equilibrium across different pressures. Moreover, as the pressure in the DDC increased, the time required for O2 to reach spatial equilibrium decreased, allowing for quicker adjustments of O2 concentration in the pressurized chamber, thereby ensuring the quality of the breathing air for divers. As shown in Fig. 5(d–f), the spatial equilibrium times for CO2 were 10 minutes, 7 minutes, and 5 minutes, respectively, with post-equilibrium concentrations of 1871.43 ppm (±0.62%), 707.14 ppm (±1.61%), and 561.23 ppm (±1.30%). The equilibrium times for both O2 and CO2 decreased as pressure increased, and the spatial distribution uniformity for CO2 in the DDC showed an RSD of no greater than 1.61%. The fluctuations in O2 and CO2 concentrations were partly due to system noise and partly due to the inherent uneven distribution of the gases. Thus, the actual RSD values for the concentration distribution at the seven spatial sampling points are likely lower than the calculated values. When the partial pressure of O2 in human breathing air exceeds 0.14 MPa, central nervous system oxygen toxicity can occur.25–27 In high-pressure environments, this high-precision, rapid mass spectrometry detection technique plays a critical role in acquiring basic data on individual tolerance and preventing oxygen toxicity.
Based on the gas equilibrium experiments conducted at 0.13 MPa, 0.6 MPa, and 1.5 MPa, we conclude that the distribution of respiratory gases (O2 and CO2) within the DDC achieves satisfactory uniformity after reaching equilibrium. The relative standard deviations in the spatial distribution of O2 did not exceed 0.34% across all pressure conditions, while CO2 showed RSDs no greater than 1.61%. These low RSD values confirm that after equilibrium is reached, personnel can move freely within the DDC while experiencing consistent respiratory conditions. The equilibrium time decreases with increasing pressure—from 5 to 1 minute for O2 and from 10 to 5 minutes for CO2—when pressure increases from 0.13 MPa to 1.5 MPa. This knowledge of equilibrium timing and distribution uniformity is crucial for establishing proper ventilation protocols and ensuring safe breathing conditions during hyperbaric operations.
Initial concentration | Adsorption time (min) | Concentration after adsorption | Concentration clearance | Removal efficiency (%) | ||
---|---|---|---|---|---|---|
1 | CO2 | 904.52 ppm | 20 | 528.59 ppm | 375.93 ppm | 39.57% |
2 | CH4 | 867.00 ppm | 60 | 773.83 ppm | 93.17 ppm | 10.75% |
3 | NH3 | 0.21 ppm | 20 | 0.18 ppm | 0.03 ppm | 14.29% |
4 | H2S | 6.57 ppb | 20 | 6.32 ppb | 0.26 ppb | 3.96% |
In this experiment, CO2 in the DDC was removed using soda lime. Prolonged exposure to low concentrations of CO2 can cause headaches, dizziness, impaired concentration, and memory loss,28,29 while short-term exposure to high concentrations of CO2 can lead to respiratory center paralysis and even death.30,31 According to the International Marine Contractors Association (IMCA) standards, each diver's oxygen consumption rate is calculated to be 0.5 L min−1, regardless of diving depth.32 A diver's respiratory quotient typically ranges from 0.7 to 1.1,33 meaning that the rate of CO2 production from a diver's respiration is between 0.35 L min−1 and 0.55 L min−1. To ensure that the partial pressure of CO2 in the decompression chamber remains within a reasonable range, the CO2 removal rate in the simulation chamber must be no less than 0.55 L min−1. As shown in Table 2, the CO2 removal efficiency was 39.57%, with a removal rate of 0.65 L min−1, which exceeds the required rate of 0.55 L min−1.
In this experiment, CH4 in the simulation chamber was removed using specially designed activated carbon. The CH4 in the DDC is produced by human metabolism. Table 2 shows that the CH4 removal efficiency was 10.75%, with a removal rate of 0.05 L min−1. Although CH4 is non-toxic, it can act as an asphyxiant at high concentrations. To increase the CH4 removal rate, the amount of CH4 adsorbent could be increased. Activated carbon was also used in this experiment to remove NH3 and H2S, both of which are toxic and odorous gases. Inhaling these gases can affect the physiological health and emotional stability of divers. According to China's national standards for diving breathing gases (GB-18435-2007), the NH3 concentration in the chamber must be less than or equal to 0.68 ppm, and the H2S concentration must be less than or equal to 4.83 ppb. As shown in Table 2, the current absorption conditions effectively remove NH3, but the efficiency of H2S removal needs to be improved. The results indicate that further enhancements are necessary to improve H2S removal efficiency.
Footnotes |
† Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d5an00132c |
‡ These authors are contributed equally to this work. |
This journal is © The Royal Society of Chemistry 2025 |