Factors Affecting CO2 Absorption in Water Using a Gas Absorption Packed Column

Maitha Zuhair Al Hadhrami, Mohammad Abdel Fattah Alalaween, Antonio Lugay Mateo, Abdulmajeed Abdulla Al Blooshi, Khalid Yousuf Kahoor, Saeed Ali Al Yileili, Rashid Salem Al Suwaidi
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Abstract

Population growth is directly associated with increase in energy demand. Amplification in industrial activity has led to a drastic escalation in greenhouse gas emissions causing global warming. The major gas involves carbon dioxide, accounting for 76% emitted from different industrial sectors. The oil and gas industry alone is responsible for 90% of these emissions. Removing CO2 is a vital process in the gas industry which must be undertaken. Carbon capture utilization and storage (CCUS) technologies have evolved through the years due to the necessity of the current world-wide shared goal, to attain net zero. Several combustion methods have been developed to capture CO2 during actual operations at fossil fuel power plants, at natural gas processing plants and at coal gasification plants. However, methods that are based on chemical and physical absorptions have been most widely used. One example is the gas absorption-based method which requires low energy consumption and has been proven to be cost-effective. Using certain water types, mixed with minute concentration of chemical solvent, it can readily absorb CO2. This approach will be used in the following research study to investigate gas absorption rate using different water samples that pass through a packed column, thereby enhancing the mass transfer of gas component. In this study, the gas absorption experiments were carried out using SOLTEQ gas absorption unit containing DN 80 packed column with glass Raschig rings and with an effective column height of 1000 mm (Figure 1). Under constant operating conditions, the temperature and pressure were set to 24°C and 2 bars, respectively, to investigate the impact of pH level and conductivity of various types of water on CO2 absorption at different gas flow rate. The statistical analysis indicates that TDS and conductivity have a stronger correlation with gas absorption (P=0.99) than pH (P=0.76). The average CO2 absorption of the three samples at different flow rates (e.g., 0.8, 1.3, and 2.2 LPM) ranged from 36.40 in sample 1 to 69.50 in sample 2 at flow rate 2.2 LPM. Overall, samples 2 and 3, neutral to base with pH value of 7.25 and 8, respectively, have a statistically significant negative correlation with average CO2 absorption, whereas the acidic (pH = 5.42) sample 1 has significant positive correlation between the two variables (R2 = 0.99). Overall, samples 2 and 3, which are neutral to base with pH values of 7.25 and 8, have a statistically significant negative correlation with average CO2 absorption. In contrast, the acidic (pH = 5.42) sample 1 has a significant positive correlation between the two variables (R2= 0.99). This study provides optimal operating conditions for the CO2 absorption process. However, additional research is required to investigate the effect of other physical and chemical properties of water on CO2 absorption.
影响气体吸收填料塔吸收水中CO2的因素
人口增长与能源需求的增加直接相关。工业活动的扩大导致温室气体排放的急剧增加,导致全球变暖。主要气体包括二氧化碳,占不同工业部门排放的76%。仅石油和天然气行业的排放量就占到其中的90%。在天然气工业中,去除二氧化碳是一个必须进行的重要过程。碳捕获、利用和封存(CCUS)技术多年来不断发展,这是由于当前全球实现净零排放的共同目标的必要性。在化石燃料发电厂、天然气处理厂和煤气化厂的实际操作中,已经开发了几种燃烧方法来捕获二氧化碳。然而,基于化学和物理吸收的方法得到了最广泛的应用。一个例子是基于气体吸收的方法,它需要低能耗,并已被证明是具有成本效益的。采用一定的水型,与微量的化学溶剂混合,可以很容易地吸收二氧化碳。这种方法将在接下来的研究中使用,通过不同的水样通过填充柱来研究气体的吸收率,从而增强气体组分的传质。在本研究中,气体吸收实验采用SOLTEQ气体吸收装置进行,该装置含有dn80填充柱,带玻璃拉希环,有效柱高为1000 mm(图1)。在恒定的操作条件下,温度和压力分别设置为24℃和2 bar,研究不同气体流速下不同类型水的pH值和电导率对CO2吸收的影响。统计分析表明,TDS和电导率与气体吸收的相关性(P=0.99)强于pH (P=0.76)。三种样品在不同流速下(如0.8、1.3和2.2 LPM)的平均CO2吸收量从样品1的36.40到样品2在2.2 LPM流速下的69.50不等。总体而言,样品2和3分别为pH值为7.25和8的中性对碱性样品,与平均CO2吸收量呈显著负相关,而酸性样品1 (pH = 5.42)与平均CO2吸收量呈显著正相关(R2 = 0.99)。总体而言,样品2和3的pH值分别为7.25和8,对碱呈中性,与平均CO2吸收量呈显著负相关。相反,酸性(pH = 5.42)样品1与两个变量之间存在显著的正相关(R2= 0.99)。本研究为CO2吸收工艺提供了最佳操作条件。然而,还需要进一步研究水的其他物理和化学性质对二氧化碳吸收的影响。
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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