Chemical Engineering and Processing - Process Intensification最新文献_第10页

Performance enhancement on the three-port gas pressure dividing device by flow channel optimization of wave rotor 通过优化波形转子的流道提高三端口气体分压装置的性能

IF 3.8 3区工程技术

Chemical Engineering and Processing - Process Intensification Pub Date : 2024-09-12 DOI: 10.1016/j.cep.2024.109972

Yawen Ji, Qing Feng, Jianli Wang, Yang Yu, Dapeng Hu

引用次数: 0

Intensified processes for CO2 capture and valorization by catalytic conversion 通过催化转化实现二氧化碳捕获和价值化的强化工艺

IF 3.8 3区工程技术

Chemical Engineering and Processing - Process Intensification Pub Date : 2024-09-12 DOI: 10.1016/j.cep.2024.109995

Maria C. Iliuta

{"title":"Intensified processes for CO2 capture and valorization by catalytic conversion","authors":"Maria C. Iliuta","doi":"10.1016/j.cep.2024.109995","DOIUrl":"10.1016/j.cep.2024.109995","url":null,"abstract":"<div>Energy and environmental issues are today's major concerns. To solve huge energy needs, the increasing use of fossil fuels leads to significant amounts of CO2 emissions, which have major negative effects on the environment. An urgent reduction in CO2 emissions is therefore an absolute priority to minimize the actual global warming. Carbon capture & utilization (CCU) has been introduced as a sustainable avenue. Viewing CO2 as a resource (renewable feedstock) rather than a waste, its conversion into different value-added products offers an attractive and efficient alternative to CO2 storage via chemical recycling. However, CO2 is a very stable molecule whose conversion is a very difficult and complex task. On the other hand, from a sustainable development perspective, CO2 conversion by catalytic hydrogenation reactions requires hydrogen derived from renewable sources. Because of numerous benefits, our group has been focussing high attention to the application of different process intensification tools to proposed technologies for CO2 capture in gas/liquid contactors (including membrane separation and enzymatic processes), highly pure hydrogen production with in-situ CO2 capture, and CO2 conversion by catalytic hydrogenation, which will be reviewed in the present paper.</div>","PeriodicalId":9929,"journal":{"name":"Chemical Engineering and Processing - Process Intensification","volume":"205 ","pages":"Article 109995"},"PeriodicalIF":3.8,"publicationDate":"2024-09-12","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142232353","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

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Integration of photocatalytic persulfate system with nanofiltration for the treatment of textile dye at pilot scale: Statistical optimization through chemometric and ridge analysis 光催化过硫酸盐系统与纳滤的整合，用于中试规模的纺织染料处理：通过化学计量学和脊分析进行统计优化

IF 3.8 3区工程技术

Chemical Engineering and Processing - Process Intensification Pub Date : 2024-09-10 DOI: 10.1016/j.cep.2024.109982

Rokia Youcef , Noureddine Bentaieb , Nadim Fakhfakh , Nassila Sabba , Padmanaban Velayudhaperumal Chellam , Amel Benhadji , Mourad Taleb Ahmed

{"title":"Integration of photocatalytic persulfate system with nanofiltration for the treatment of textile dye at pilot scale: Statistical optimization through chemometric and ridge analysis","authors":"Rokia Youcef , Noureddine Bentaieb , Nadim Fakhfakh , Nassila Sabba , Padmanaban Velayudhaperumal Chellam , Amel Benhadji , Mourad Taleb Ahmed","doi":"10.1016/j.cep.2024.109982","DOIUrl":"10.1016/j.cep.2024.109982","url":null,"abstract":"<div>The assessment of the sulfate radical-based AOPs (SR-AOPs) in an immobilized reactor combined with various methods for treating brilliant blue FCF (BBF) is presented with emphasis given to energy efficiency, sustainable development, and practicality. The SR-AOPs method, used at the pilot scale under UV light irradiation has a treatment capacity of 0.519 m3/l. It is optimized utilizing the central composite design (CCD) approach for UVA-PS-TiO2 process treatment, an empirical connection concerning removal efficiency was established by choosing as factors TiO2 concentration [0.5–2] g/l, the treatment time [30–180] min, and the concentration of S2O8 [1–3] g/l. The model's significance for the maximal BBF elimination was determined using the variance results (ANOVA) and the adequacy result of Canonical and ridge analysis was also conducted to determine optimal result. In terms of kinetics 3.89 h−1 for NF, 2.61 h−1 for UVA-PS-TiO2/NF, and 0.68 h−1 for UVA-PS-TiO2 and economic evaluation PS-TiO2 with a total cost of 572,32 €/m3 and PS-TiO2<img>NF with an operation cost of 574,28 €/m3. The integration of membrane processes (NF) with UV/ PS/TiO2 allow to reduce the total cost of process and to enhance the kinetic parameters. The technical-economic study demonstrated a successful scenario with a 23-year payback period.</div>","PeriodicalId":9929,"journal":{"name":"Chemical Engineering and Processing - Process Intensification","volume":"205 ","pages":"Article 109982"},"PeriodicalIF":3.8,"publicationDate":"2024-09-10","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142243291","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

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Valorization of glycerol to mono- and di-glycerides: Feedstocks, intensified reactors, challenges and perspectives 将甘油转化为单甘油酯和双甘油酯：原料、强化反应器、挑战和前景

IF 3.8 3区工程技术

Chemical Engineering and Processing - Process Intensification Pub Date : 2024-09-08 DOI: 10.1016/j.cep.2024.109978

Kanokwan Ngaosuwan

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Two-stage microreactor with intensely swirling flows: Comparison of three methods of liquids feeding 具有强烈漩涡流的两级微反应器：三种液体进料方法的比较

IF 3.8 3区工程技术

Chemical Engineering and Processing - Process Intensification Pub Date : 2024-09-08 DOI: 10.1016/j.cep.2024.109991

R.S. Abiev, I.V. Makusheva

{"title":"Two-stage microreactor with intensely swirling flows: Comparison of three methods of liquids feeding","authors":"R.S. Abiev, I.V. Makusheva","doi":"10.1016/j.cep.2024.109991","DOIUrl":"10.1016/j.cep.2024.109991","url":null,"abstract":"<div>A two-stage microreactor with intensely swirling flows (MRISF-2) allows to perform effectively two subsequent reactions in synthesis of nanosized particles. Micromixing quality plays crucial role in ultrafast co-precipitation reactions, and depends both on the specific energy dissipation rate and on the geometry of the reactor as well as the solutions feeding manner. Solutions in MRISF-2 could be supplied by different ways: through the upper and/or lower tangential inlet pipes and through the central (axial) inlet pipe. This paper is aimed to compare experimentally and numerically three ways of liquid solutions feeding in MRISF-2 with objective to find the conditions of the highest specific energy dissipation rate. The best method of solutions supplying was found experimentally and confirmed numerically: one solution is supplied tangentially, the other through the central inlet pipe. The average specific energy dissipation rate for this method is 1.7 and 6.0 times higher compared to supply through two upper tangential inlet pipes and upper + lower tangential inlet pipes, respectively. This advantage was confirmed by measurements of segregation index Xs by use of iodide-iodate reaction technique. Good agreement between experimental and numerical simulation results for energy dissipation rate was found for all studied cases.</div>","PeriodicalId":9929,"journal":{"name":"Chemical Engineering and Processing - Process Intensification","volume":"205 ","pages":"Article 109991"},"PeriodicalIF":3.8,"publicationDate":"2024-09-08","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142243292","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

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Hydrothermal treatment of natural rectorite enhanced Mo sulfidation for slurry-phase hydrocracking of vacuum residue 对天然雷克托石进行水热处理，增强钼硫化能力，用于真空渣浆相加氢裂化

IF 3.8 3区工程技术

Chemical Engineering and Processing - Process Intensification Pub Date : 2024-09-06 DOI: 10.1016/j.cep.2024.109983

Qingyan Cui , Jianteng Yan , Haobin Zhang , Weiwei Feng , Yuanyuan Yue , Tiesen Li , Jie Shi

{"title":"Hydrothermal treatment of natural rectorite enhanced Mo sulfidation for slurry-phase hydrocracking of vacuum residue","authors":"Qingyan Cui , Jianteng Yan , Haobin Zhang , Weiwei Feng , Yuanyuan Yue , Tiesen Li , Jie Shi","doi":"10.1016/j.cep.2024.109983","DOIUrl":"10.1016/j.cep.2024.109983","url":null,"abstract":"<div>Natural rectorite modified by the hydrothermal method was employed to prepare a catalyst for the slurry-phase hydrocracking of vacuum residue (VR). The influence of hydrothermal treatment on the properties of rectorite and the performance of the corresponding catalyst was examined. Hydrothermal treatment of the rectorite led to the formation of Fe3O4, as evidenced by H2-TPR analysis. XPS results indicate that the hydrothermal treatment of rectorite can intensify the sulfidation process of Mo species supported on it, possibly due to modifications in the surface properties of the rectorite. Comparative slurry-phase hydrocracking tests showed that the catalyst supported on hydrothermally treated rectorite exhibited significantly higher VR conversion, higher liquid product yield, and higher yields of gasoline and diesel fractions, but lower gas yield compared to the catalyst supported on untreated rectorite. This is ascribed to the high hydrogenation activity of the catalyst supported on hydrothermally treated rectorite, which effectively suppresses the over-cracking reactions of intermediate products that would otherwise produce gas, illustrating the process intensification achieved through hydrothermal treatment.</div>","PeriodicalId":9929,"journal":{"name":"Chemical Engineering and Processing - Process Intensification","volume":"205 ","pages":"Article 109983"},"PeriodicalIF":3.8,"publicationDate":"2024-09-06","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142164868","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

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Design and optimisation of lysozyme protein purification process using non-thermal progressive freeze concentration technology 利用非热渐进式冷冻浓缩技术设计和优化溶菌酶蛋白纯化工艺

IF 3.8 3区工程技术

Chemical Engineering and Processing - Process Intensification Pub Date : 2024-09-06 DOI: 10.1016/j.cep.2024.109975

Tazien Rashid , Mazura Jusoh , Zaki Yamani Zakaria , Norshafika Yahya , Sabah Ansar , Tiong Sieh Kiong , Farooq Sher

{"title":"Design and optimisation of lysozyme protein purification process using non-thermal progressive freeze concentration technology","authors":"Tazien Rashid , Mazura Jusoh , Zaki Yamani Zakaria , Norshafika Yahya , Sabah Ansar , Tiong Sieh Kiong , Farooq Sher","doi":"10.1016/j.cep.2024.109975","DOIUrl":"10.1016/j.cep.2024.109975","url":null,"abstract":"<div>In this study, PFC system is investigated to improve the concentration and yield of lysozyme. The research focused on an attempt to thoroughly construct an ice crystallizer with measurable and optimized design parameters for an efficient lysozyme protein concentration procedure because the productivity of PFC is always an issue. A new Multiple Probe Cryo-Concentrator (MPCC) device was designed and successfully equipped with probes having a well-distributed cooled surface area for ice crystallization with proper internal cooling temperature control as well as a solution movement mechanism provided by a stirrer in the tank. The impact of different operating parameters is optimally investigated. Central Composite Design (CCD) is utilized to optimize PFC operating conditions and their response to partition constant (K-value) and solute yield. The results showed that a coolant temperature of -12 ⁰C, stirrer speed of 350 rpm, operation time of 40 min and initial concentration of 10 mg/mL gave the best K-value (0.132) and solute concentration yield (87.39 %). The design elements of the equipment are crucial in providing improved PFC performance. The study revealed that the PFC system designed and applied in this study can improve the lysozyme protein concentration as needed in the food and pharmaceutical industry.</div>","PeriodicalId":9929,"journal":{"name":"Chemical Engineering and Processing - Process Intensification","volume":"205 ","pages":"Article 109975"},"PeriodicalIF":3.8,"publicationDate":"2024-09-06","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://www.sciencedirect.com/science/article/pii/S0255270124003131/pdfft?md5=d10cd7b96771a43754d302c89f7794cb&pid=1-s2.0-S0255270124003131-main.pdf","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142243293","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

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Experimental study of high-pressure ultrasound-assisted oxidative desulfurization (UAOD) and sulfone adsorption/desorption using zeolite-13X 使用沸石-13X 进行高压超声辅助氧化脱硫（UAOD）和砜吸附/脱附的实验研究

IF 3.8 3区工程技术

Chemical Engineering and Processing - Process Intensification Pub Date : 2024-09-05 DOI: 10.1016/j.cep.2024.109964

Mohammad Reza Zaeri, Feridun Esmaeilzadeh

{"title":"Experimental study of high-pressure ultrasound-assisted oxidative desulfurization (UAOD) and sulfone adsorption/desorption using zeolite-13X","authors":"Mohammad Reza Zaeri, Feridun Esmaeilzadeh","doi":"10.1016/j.cep.2024.109964","DOIUrl":"10.1016/j.cep.2024.109964","url":null,"abstract":"<div>The sulfurous compounds in natural gas liquids should be reduced to the extent of satisfying the standard recipes due to corrosion, poisoning of catalysts in downstream processes, reduction in the quality of hydrocarbon products and environmental issues. Ultrasound-assisted oxidative desulfurization is an emerging method for sulfur removal from natural gas liquids. Since natural gas liquids exist in the liquid form of hydrocarbons at high pressures and ambient temperature (25 °C), this work aims to investigate the optimal conditions governing ultrasound-assisted oxidative desulfurization for various sulfurous compounds including mercaptan, sulfide and thiophene at high pressure and finally to appraise the adsorption of oxidized sulfurs and the regeneration of the adsorbent using elution with hot water. So, the effects of sulfur content and ultrasonication time were evaluated at 30 bar. Results showed that as the initial sulfur concentration in normal heptane was increased from 0.00 to 3000 ppmS, the sulfur removal efficiency was enhanced by less than 2 % of 95.9 % and of course, the increased ultrasonication time improved the sulfur removal efficiency. Next, results of the sulfone adsorption using zeolite-13X at 30 bar in continuous mode confirmed that the breakthrough time was reduced from 63 to 12 min as the weight hourly space velocity was increased from 5 to 20 h−1 and pursuantly, the mass transfer zone diminished. Besides, the breakthrough time decreased by 45 - 10 min for increasing the initial sulfur content from 200 to 1000 ppmS. Changing the pressure of the adsorption process from 1 to 30 bar caused the improvement of sulfone adsorption capacity by approximately 3.75 times. In continued, the regeneration of zeolite-13X contaminated with sulfone by flowing hot water was evaluated and the zeolite-13X bed was completely regenerated.</div>","PeriodicalId":9929,"journal":{"name":"Chemical Engineering and Processing - Process Intensification","volume":"205 ","pages":"Article 109964"},"PeriodicalIF":3.8,"publicationDate":"2024-09-05","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142172549","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

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Processing technologies of oil and gas based on molecular refining: Separation and conversion 基于分子精炼的石油和天然气加工技术：分离和转化

IF 3.8 3区工程技术

Chemical Engineering and Processing - Process Intensification Pub Date : 2024-09-05 DOI: 10.1016/j.cep.2024.109968

Liang Zhao, Dongyang Liu, Yuhao Zhang, Jinsen Gao, Chunming Xu

{"title":"Processing technologies of oil and gas based on molecular refining: Separation and conversion","authors":"Liang Zhao, Dongyang Liu, Yuhao Zhang, Jinsen Gao, Chunming Xu","doi":"10.1016/j.cep.2024.109968","DOIUrl":"10.1016/j.cep.2024.109968","url":null,"abstract":"<div>Driven by the goal of carbon neutrality, the new development pattern of the refining and chemical industry has changed from distillate processing to component processing. A key difficulty in precise separation of oil and gas is a low separation efficiency, which could be attributed to poor gas-liquid mass transfer efficiency and poor match between selectivity and solubility. While in the oriented conversion of oil, low yield of the target product and short catalyst life are key constraints, since complex parallel sequence reactions in conversion process is difficult to control. Therefore, our research group has focused on the main line of \"precise separation and oriented conversion of oil and gas\", to cope with a key chemical common problems of \"mass transfer and reaction\" in the process of \"separation and conversion\" of C3-C20 hydrocarbon components, we solved two scientific problems of \"intermolecular force\" in separation process and \"structure-activity relationship of catalytic materials\" in conversion process. It has realized the goal of \"quality upgrade, product transformation and optimal utilization\" mainly for production of high-quality fuel and chemical feedstocks. And it has contributed to form a new pattern of refining and chemical integration of \"high-qualified oil and gas as well as high-value chemicals\".</div>","PeriodicalId":9929,"journal":{"name":"Chemical Engineering and Processing - Process Intensification","volume":"205 ","pages":"Article 109968"},"PeriodicalIF":3.8,"publicationDate":"2024-09-05","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142164662","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

引用次数: 0

Preparation and pipeline transport of CO2 as a hydrate slurry – Modelling and techno-economic analysis 二氧化碳水合物泥浆的制备和管道运输 - 建模和技术经济分析

IF 3.8 3区工程技术

Chemical Engineering and Processing - Process Intensification Pub Date : 2024-09-05 DOI: 10.1016/j.cep.2024.109973

Isabel S. Fernandes , Mariana G. Domingos , Marcelo F. Costa , Ricardo J. Santos , José Carlos B. Lopes

{"title":"Preparation and pipeline transport of CO2 as a hydrate slurry – Modelling and techno-economic analysis","authors":"Isabel S. Fernandes , Mariana G. Domingos , Marcelo F. Costa , Ricardo J. Santos , José Carlos B. Lopes","doi":"10.1016/j.cep.2024.109973","DOIUrl":"10.1016/j.cep.2024.109973","url":null,"abstract":"<div>CO2 transportation as a hydrate slurry is modelled in Aspen Plus, including the slurry preparation and the pipeline transport. Due to the lack of built-in models for the hydrate formation, mass and energy balances were developed and implemented using a User-block function. NRTL-RK global property method was used, given the accuracy in predicting the CO2 solubility in water under incipient hydrate formation conditions and the dissolution heat of CO2 in water. The conventional process of transporting CO2 in a supercritical state was also modelled to benchmark the hydrate-based technology. The hydrate-based process is safer than the conventional process as it requires lower operating pressures, but the estimated costs are higher due to the need for refrigeration and larger pipeline diameters for transportation. The addition of thermodynamic promoters, that moderate the hydrate formation conditions, the integration of cold streams with other processes, and valuing the water transported with CO2, will enhance the economic attractiveness of the hydrate-based process.</div>","PeriodicalId":9929,"journal":{"name":"Chemical Engineering and Processing - Process Intensification","volume":"205 ","pages":"Article 109973"},"PeriodicalIF":3.8,"publicationDate":"2024-09-05","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://www.sciencedirect.com/science/article/pii/S0255270124003118/pdfft?md5=d7a77942271342a1b5a0d98b9f9a3922&pid=1-s2.0-S0255270124003118-main.pdf","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142272379","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

引用次数: 0