{"title":"Solvent extraction and supercritical water oxidation; A hybrid method for oil sludge remediation","authors":"Saeed Rahimi Hardorodee , Ahmad Hallajisani , Roya Mafigholami , Karim Ghasemipanah","doi":"10.1016/j.jwpe.2025.108729","DOIUrl":null,"url":null,"abstract":"<div><div>In this research, a dual approach involving solvent extraction and supercritical water oxidation was employed to recover and enhance oil sludge. Initially, for the solvent extraction phase, experiments were performed utilizing Design Expert software to analyze the impact of temperature settings ranging from 25 to 50 °C, duration between 10 and 30 min, and a solvent-to-sludge ratio varying from 2 to 8. Additionally, the influence of using different solvents, specifically ethanol and hexane, for hydrocarbon extraction from the sludge was examined. The experimental findings indicated that the ideal conditions for solvent extraction were a temperature of 35 °C, a duration of 20 min, and a solvent-to-sludge ratio of 5.5, under which the solvents successfully separated 68 % of the petroleum hydrocarbons present in the oil sludge sample. In the subsequent phase, the supercritical water oxidation process was implemented to recover and enhance the quality of the resultant products. The experimental design was executed using response surface methodology, under the following parameters: temperature between 390 and 450 °C, duration of 30 to 90 min, a water-to-feed ratio of 1 to 5, and a hydrogen-to-feed ratio of 2 to 1. Among these variables, the water-to-feed ratio was found to have the most significant impact on the efficiency of the supercritical oxidation process. The optimal conditions were identified as a temperature of 420 °C, a duration of 60 min, and a water-to-feed ratio of 3, under which 64 % of hydrocarbon compounds were recovered. The presence of water enhances the concentration of OH radicals, thereby increasing the reaction rate, which ultimately boosts the yield of recovered products. In the final stage, the influence of various weight ratios of zeolite catalyst (5, 50, 20, 10, and 100 %) was assessed to improve product quality. The test results revealed that at a catalyst ratio of 10 %, 84 % of the products were successfully recovered. The findings of this research demonstrate that the integration of solvent extraction and supercritical catalytic oxidation with water is both effective and efficient in recovering hydrocarbons from oil sludge.</div></div>","PeriodicalId":17528,"journal":{"name":"Journal of water process engineering","volume":"78 ","pages":"Article 108729"},"PeriodicalIF":6.7000,"publicationDate":"2025-09-11","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Journal of water process engineering","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S2214714425018021","RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
引用次数: 0
Abstract
In this research, a dual approach involving solvent extraction and supercritical water oxidation was employed to recover and enhance oil sludge. Initially, for the solvent extraction phase, experiments were performed utilizing Design Expert software to analyze the impact of temperature settings ranging from 25 to 50 °C, duration between 10 and 30 min, and a solvent-to-sludge ratio varying from 2 to 8. Additionally, the influence of using different solvents, specifically ethanol and hexane, for hydrocarbon extraction from the sludge was examined. The experimental findings indicated that the ideal conditions for solvent extraction were a temperature of 35 °C, a duration of 20 min, and a solvent-to-sludge ratio of 5.5, under which the solvents successfully separated 68 % of the petroleum hydrocarbons present in the oil sludge sample. In the subsequent phase, the supercritical water oxidation process was implemented to recover and enhance the quality of the resultant products. The experimental design was executed using response surface methodology, under the following parameters: temperature between 390 and 450 °C, duration of 30 to 90 min, a water-to-feed ratio of 1 to 5, and a hydrogen-to-feed ratio of 2 to 1. Among these variables, the water-to-feed ratio was found to have the most significant impact on the efficiency of the supercritical oxidation process. The optimal conditions were identified as a temperature of 420 °C, a duration of 60 min, and a water-to-feed ratio of 3, under which 64 % of hydrocarbon compounds were recovered. The presence of water enhances the concentration of OH radicals, thereby increasing the reaction rate, which ultimately boosts the yield of recovered products. In the final stage, the influence of various weight ratios of zeolite catalyst (5, 50, 20, 10, and 100 %) was assessed to improve product quality. The test results revealed that at a catalyst ratio of 10 %, 84 % of the products were successfully recovered. The findings of this research demonstrate that the integration of solvent extraction and supercritical catalytic oxidation with water is both effective and efficient in recovering hydrocarbons from oil sludge.
期刊介绍:
The Journal of Water Process Engineering aims to publish refereed, high-quality research papers with significant novelty and impact in all areas of the engineering of water and wastewater processing . Papers on advanced and novel treatment processes and technologies are particularly welcome. The Journal considers papers in areas such as nanotechnology and biotechnology applications in water, novel oxidation and separation processes, membrane processes (except those for desalination) , catalytic processes for the removal of water contaminants, sustainable processes, water reuse and recycling, water use and wastewater minimization, integrated/hybrid technology, process modeling of water treatment and novel treatment processes. Submissions on the subject of adsorbents, including standard measurements of adsorption kinetics and equilibrium will only be considered if there is a genuine case for novelty and contribution, for example highly novel, sustainable adsorbents and their use: papers on activated carbon-type materials derived from natural matter, or surfactant-modified clays and related minerals, would not fulfil this criterion. The Journal particularly welcomes contributions involving environmentally, economically and socially sustainable technology for water treatment, including those which are energy-efficient, with minimal or no chemical consumption, and capable of water recycling and reuse that minimizes the direct disposal of wastewater to the aquatic environment. Papers that describe novel ideas for solving issues related to water quality and availability are also welcome, as are those that show the transfer of techniques from other disciplines. The Journal will consider papers dealing with processes for various water matrices including drinking water (except desalination), domestic, urban and industrial wastewaters, in addition to their residues. It is expected that the journal will be of particular relevance to chemical and process engineers working in the field. The Journal welcomes Full Text papers, Short Communications, State-of-the-Art Reviews and Letters to Editors and Case Studies