Chemical Engineering and Processing-Process Intensification化学工程与加工——过程强化

Chemical Engineering and Processing-Process Intensification(英文缩写 CHEM ENG PROCESS),ISSN 0255-2701,eISSN 1873-3204,中文译名:化学工程与加工——过程强化 是一本学术期刊。本页汇总该期刊的最新影响因子、分区信息以及最新收录于 PubMed 的文献,帮助您快速了解期刊全貌。

2026 年数据 · 影响因子
4.200
JCR 分区
Q2
CAS 分区
B3
近一年发文量
0
本站 PubMed 收录统计

发文量统计区间:2025-09-27 至 2026-09-27,按本站收录文献的发表日期统计。

ISSN: 0255-2701 · eISSN: 1873-3204 · 缩写: CHEM ENG PROCESS ·中文: 化学工程与加工——过程强化

期刊介绍

选择期刊介绍栏目

期刊简介

《Chemical Engineering and Processing-Process Intensification》是化学工程领域聚焦过程强化与工艺工程的国际期刊,涵盖反应、分离、传热传质等单元操作的强化原理与工程实现。读者群主要为化工、能源与环境领域的科研人员、工艺开发工程师及研究生,强调从实验室到工业放大的衔接,关注可持续与高效流程创新。

研究方向

主要方向包括过程强化技术、微反应器与结构化反应器、膜与吸附分离、多相传递、过程集成与节能、以及化工过程的建模、优化与放大。论文类型以原创研究、综述和工程案例为主,兼收短讯与评论,鼓励实验与模拟结合的工作。

期刊特色

研究取向偏应用基础与工程验证,重视新概念装置、强化机制和可放大性,论文通常要求清晰的实验数据或可靠模型支撑。适合化工工艺研发、过程系统工程师及希望将实验室成果推向中试与工业应用的研究者阅读与投稿。

投稿难度

投稿难度中等偏上,对创新性和工程价值要求较高,仅凭分区不能判断录用难易。建议突出过程强化的新意、提供充分的对比实验与放大分析,并注意语言表达与图表规范,以提升送审与接收机会。

历年影响因子趋势

JCR 数据年份影响因子JCR 分区
20214.264Q2
20224.300Q2
20233.800Q2
20243.900Q2
20254.200Q2

Chemical Engineering and Processing-Process Intensification 最新收录文献

  1. JCR分区: Q2 CAS分区: B3 影响因子: 4.2

    1. Continuous Extraction of 2-Chloroethyl isocyanate for 1-(2-chloroethyl)-3-cyclohexylurea Purification.

    作者:
    Jaron Mackey, Devna Grover, Gabriella Pruneda, Eva Zenk, Zoltan K Nagy
    日期:
    2023-01-01

    This study details the development of simulation-aided design, development, and successful operation of a continuous liquid-liquid extraction platform made with 1.5 mm tubing for the extraction of 2-chloroethyl isocyanate, an important reagent in the synthesis of cancer drugs. Preliminary solvent screening was carried out with partition coefficient calculations to determine solvents of interest. Next, batch and flow extraction experiments of 2-chloroethyl isocyanate in 2-methyl tetrahydrofuran and water were conducted to estimate extraction parameters. Following parameter estimation, experimental and model values for Ka were determined in the range of 1.13×10 to 36.0×10 s. Simulations of the extraction of 2-chloroethyl isocyanate were found to agree with experimental data resulting in a maximum efficiency of 77% and percent extraction of 69% for the continuous platform. Finally, model selection and discrimination was implemented for design space generation with experimental and model determined Ka values to guide lab-scale operation.

  2. JCR分区: Q2 CAS分区: B3 影响因子: 4.2

    2. Optimal waste management during the COVID-19 pandemic.

    作者:
    Aurora Del Carmen Munguía-López, Rogelio Ochoa-Barragán, José María Ponce-Ortega
    日期:
    2022-06-01

    There have been many problems generated by the COVID-19 pandemic. One of them is the worrying increase in the generation of medical waste due to the great risk they represent for health. Therefore, this work proposes a mathematical model for optimal solid waste management, proposing a circular value chain where all types of waste are treated in an intensified industrial park. The model selects the processing technologies and their production capacity. The problem was formulated as a mixed-integer linear programming problem to maximize profits and the waste processed, minimizing environmental impact. The proposed strategy is applied to the case study of the city of New York, where the increase in the generation of medical waste has been very significant. To promote recycling, different tax rates are proposed, depending on the amount of waste sent to the landfill. The results are presented on a Pareto curve showing the trade-off between profits and processed waste. We observed that the taxes promote recycling, even of those wastes that are not very convenient to recycle (from an economic point of view), favoring profits, reducing the environmental impact, and the risk to health inherent to the medical waste.

  3. JCR分区: Q2 CAS分区: B3 影响因子: 4.2

    3. Spiral column configuration for protein separation by high-speed countercurrent chromatography.

    作者:
    Yoichiro Ito
    日期:
    2010-07-01

    Retention of the stationary phase of aqueous-aqueous polymer phase systems is improved by a spiral column configuration which utilizes the radially acting centrifugal force along the spiral pitch to retain the heavier phase in the outer portion and the lighter phase in the inner portion of the spiral channel. For the separation of proteins which has low mass transfer rates, the system needs further modification of the separation channel to interrupt the laminar flow and enhance mixing of the two phases. Two spiral column assemblies were developed, one using a disk with spiral grooves and the other, the spiral tube support which accommodates the multiple spiral layers made from a single piece of fluorinated plastic tubing. In the spiral disk assembly, the best protein separation is achieved by the mixer-settler system which vigorously mixes two phases by vibrating glass beads placed in every other section of barricaded spiral channel, while in the spiral tube assembly the partition efficiency of proteins is enhanced by compressing the tubing to interrupt the laminar flow of the mobile phase. In both systems protein samples were well resolved by choosing the suitable elution modes.

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