Purification of Industrial Effluent by Gas Hydrate-based (HyPurif) Process

被引:5
作者
Sharma, Subhash Kumar [1 ]
Bhadauria, Anshu [1 ]
Kumar, T. Nanda [2 ]
Kumar, Rajnish [1 ]
机构
[1] Indian Inst Technol Madras, Dept Chem Engn, NAC449, Chennai 600036, India
[2] Gail India Ltd, DGM R&D Projects Select Execut & Management, Noida 201301, Uttar Pradesh, India
关键词
Gas hydrate; Wastewater purification; Industrial effluents; Clathrate process; Cyclopentane; Nitrogen; HFC; 134a; Propane; SEAWATER DESALINATION; CARBON-DIOXIDE; PHASE-EQUILIBRIUM; SALT REMOVAL; WATER; ENERGY; INTERFACE; HYDROGEN; IONS;
D O I
10.1016/j.jclepro.2023.138424
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This study presents a sustainable HyPurif process for managing and recycling industrial water effluent, utilizing gas hydrate-based technology to purify complex effluent. This work purifies two effluents: one from a wastewater treatment plant (WWTP) and the other from a spent caustic treatment plant (SCTP). Various hydrate formers, including propane, HFC134a, and cyclopentane (6 mol %), were selected, as they typically form hydrates closer to ambient conditions. Hydrate formation experiments with effluent water were performed at 278.30 K using pure propane and HFC134a gas. Based on the kinetics of hydrate growth, the study was extended to a mixture (50:50%) of propane and HFC134a, operating at a pressure of 0.6 MPa. The mixture of propane and HFC134a has shown the desired result of forming the hydrate in the gas phase and having high separation efficiency. The results showed that the formation and dissociation of hydrates resulted in a separation efficiency of 80-95%. For instance, in the purified water, the biological oxygen demand (BOD) decreased from 2097 mg/L in the effluent sample to 220 mg/L in purified water (purification efficiency of 90.5%). The chemical oxygen demand (COD) decreased from 3100 mg/L in the effluent sample to 503 mg/L in purified water (purification efficiency of 84%). Total dissolved solids (TDS) were reduced from 89,632 mg/L in the effluent water to 14,698 mg/L in purified water (purification efficiency of 84%). Total suspended solids (TSS) were reduced from 35 mg/L in the effluent water to 3.5 mg/L in purified water (purification efficiency of 90%). However, the purification efficiency for free ammonia and residual chlorine was lower. The concentration of free ammonia decreased from 7 mg/L in the effluent sample to 1.89 mg/L in the purified water (purification efficiency of 73%), and residual chlorine reduced from 0.8 mg/L in the effluent sample to 0.2 mg/L in the purified water (purification efficiency of 75%). Water recovery of >= 40% was achievable per pass, which could be increased, but at the expense of purification efficiency. To the best of our knowledge, this is the first study on the purification of such complex wastewater containing organic and inorganic compounds, heavy metals, and various minerals using the HyPurif process.
引用
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页数:14
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