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Effects of acid-rock reaction on physical properties during CO_(2)-rich industrial waste gas(CO_(2)-rich IWG)injection in shale reservoirs
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作者 Yi-Fan Wang Jing Wang +2 位作者 Hui-Qing Liu Xiao-Cong Lv Ze-Min Ji 《Petroleum Science》 SCIE EI CAS CSCD 2024年第1期272-285,共14页
"Carbon peaking and carbon neutrality"is an essential national strategy,and the geological storage and utilization of CO_(2)is a hot issue today.However,due to the scarcity of pure CO_(2)gas sources in China... "Carbon peaking and carbon neutrality"is an essential national strategy,and the geological storage and utilization of CO_(2)is a hot issue today.However,due to the scarcity of pure CO_(2)gas sources in China and the high cost of CO_(2)capture,CO_(2)-rich industrial waste gas(CO_(2)-rich IWG)is gradually emerging into the public's gaze.CO_(2)has good adsorption properties on shale surfaces,but acidic gases can react with shale,so the mechanism of the CO_(2)-rich IWG-water-shale reaction and the change in reservoir properties will determine the stability of geological storage.Therefore,based on the mineral composition of the Longmaxi Formation shale,this study constructs a thermodynamic equilibrium model of water-rock reactions and simulates the regularity of reactions between CO_(2)-rich IWG and shale minerals.The results indicate that CO_(2)consumed 12%after reaction,and impurity gases in the CO_(2)-rich IWG can be dissolved entirely,thus demonstrating the feasibility of treating IWG through water-rock reactions.Since IWG inhibits the dissolution of CO_(2),the optimal composition of CO_(2)-rich IWG is 95%CO_(2)and 5%IWG when CO_(2)geological storage is the main goal.In contrast,when the main goal is the geological storage of total CO_(2)-rich IWG or impurity gas,the optimal CO_(2)-rich IWG composition is 50%CO_(2)and 50%IWG.In the CO_(2)-rich IWG-water-shale reaction,temperature has less influence on the water-rock reaction,while pressure is the most important parameter.SO2 has the greatest impact on water-rock reaction in gas.For minerals,clay minerals such as illite and montmorillonite had a significant effect on water-rock reaction.The overall reaction is dominated by precipitation and the volume of the rock skeleton has increased by 0.74 cm3,resulting in a decrease in shale porosity,which enhances the stability of CO_(2)geological storage to some extent.During the reaction between CO_(2)-rich IWG-water-shale at simulated temperatures and pressures,precipitation is the main reaction,and shale porosity decreases.However,as the reservoir water content increases,the reaction will first dissolve and then precipitate before dissolving again.When the water content is less than 0.0005 kg or greater than 0.4 kg,it will lead to an increase in reservoir porosity,which ultimately reduces the long-term geological storage stability of CO_(2)-rich IWG. 展开更多
关键词 CO_(2)-rich industrial waste gas Geological storage Acid-rock reaction SHALE Geochemical modelling
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含钙工业废渣在烟气干法脱硫中的应用及改性 被引量:2
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作者 马晓宇 王歆銘 +3 位作者 崔素萍 王亚丽 王剑锋 吴红 《北京工业大学学报》 CAS CSCD 北大核心 2022年第9期998-1008,共11页
SO是污染大气、危害健康、造成经济损失的主要污染气体,也是水泥窑等大型工业生产过程中排出的一种主要的废气,严重地影响着人们的生活.在目前的脱硫方法中,干法脱硫无废渣废水产生,热损耗低,有利于节能减排,是目前最环保的方法之一,众... SO是污染大气、危害健康、造成经济损失的主要污染气体,也是水泥窑等大型工业生产过程中排出的一种主要的废气,严重地影响着人们的生活.在目前的脱硫方法中,干法脱硫无废渣废水产生,热损耗低,有利于节能减排,是目前最环保的方法之一,众多干法脱硫剂中钙基脱硫剂因其资源丰富、使用简便占据重要地位.含钙工业废渣由于钙含量高或富含金属氧化物及SiO_(2)等成分,被用于钙基脱硫剂的制备与改性,提高干法脱硫性能.综述了含钙工业废渣制备和改性干法脱硫钙基脱硫剂的现有研究,并通过分析改性机理及脱硫反应过程,对提高含钙工业废渣脱硫性能的改性方法进行了讨论. 展开更多
关键词 SO_(2) 干法脱硫 钙基脱硫剂 改性 工业废渣 金属氧化物
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Preparation of gangue ceramsite by sintering pot test and potential analysis of waste heat recovery from flue gas 被引量:2
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作者 Yi Huang Xiang-jie Duan +1 位作者 Yu Li Wei Zhang 《Journal of Iron and Steel Research International》 SCIE EI CAS CSCD 2023年第7期1401-1410,共10页
Preparation of ceramsite from solid waste based on the sintering process is a new technology and had a high efficiency in improving producing capability, decreasing consumption of liquefied petroleum gas (LPG), and re... Preparation of ceramsite from solid waste based on the sintering process is a new technology and had a high efficiency in improving producing capability, decreasing consumption of liquefied petroleum gas (LPG), and recovering waste heat of flue gas. An experiment sintering gangue ceramsite was conducted in a 25 kg scale sintering pot with a 100 cm height. The combustion characteristics, phase transformation, and the release profile of SO_(2)^(*) (SO and/or SO_(2)) and NO_(x)^(*) (N_(2)O, NO, and/or NO_(2)) of gangue ceramsite during the sintering process were studied by X-ray diffraction analysis, X-ray fluorescence spectrometry, thermogravimetry–differential thermogravimetry–differential scanning calorimetry, and measurement of physical properties of ceramsite and gas components of flue gas. The results showed that the gangue ceramsite had excellent properties, and its compressive strength and water absorption were 8.2–9.6 MPa and 8.9%–9.8%, respectively, far exceeding the requirement of standard (GB/T 17431.1–2010). The ignition temperature of gangue ceramsite was 443 ℃, and the ignition loss was 14.60 mass% at 1000 ℃. Kaolinite and calcite disappeared at 600 and 800 ℃, respectively. Albite disappeared and mullite formed at 1000 ℃. Two peaks of SO_(2)^(*) emissions emerged in the range of 311–346 mg m^(-3) near 500 ℃ of upper layer ceramsite and 420–489 mg m^(-3) near 1000 ℃ of lower layer ceramsite, respectively. NO_(x)^(*) emissions peak emerged in the range of 227–258 mg m^(-3) near 550 ℃ of the upper layer ceramsite, which was related to the oxidation of sulfide and the combustion of LPG. Gangue is a direct heat source for sintering of ceramsite as well. During sintering process, the heat of flue gas above and below 400 ℃ accounts for 55.9% and 30.0% of the all-output heat, respectively, and was potentially used for producing waste-heat steam or electricity as by-products and drying raw materials during its own initial sintering process, which can realize combined mass and heat utilization for the gangue and further reduce the cost of sintered gangue ceramsite. 展开更多
关键词 Gangue ceramsite COGENERATION SO_(2)^(*) NO_(x)^(*) Flue gas waste heat
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