Modeling and Optimization of Distillation Column for Separation of 18O Isotope with Mathematical Model

被引:0
|
作者
Ahmadi, H. [1 ]
Rahgoshay, M. [1 ]
Heydarinasab, A. [2 ]
机构
[1] Islamic Azad Univ, Fac Engn, Dept Nucl Engn, Sci & Res Branch, Tehran, Iran
[2] Islamic Azad Univ, Fac Petr & Chem Engn, Dept Chem Engn, Sci & Res Branch, Tehran, Iran
关键词
Oxygen separation; distillation column; fluorodeoxyglucose; PET imaging; POSITRON-EMISSION-TOMOGRAPHY; FDG PET;
D O I
10.1080/00295639.2024.2440684
中图分类号
TL [原子能技术]; O571 [原子核物理学];
学科分类号
0827 ; 082701 ;
摘要
Positron emission tomography (PET) is an advanced imaging tool for the diagnosis and staging of cancer tumors. This method is based on the detection of increased glycolytic activity in malignant cells, in which cell glucose is concentrated because of an increase in membrane glucose transporters, as well as an increase in some key enzymes, such as hexokinase, which are responsible for glucose phosphorylation. Therefore, for this type of imaging, drugs containing glucose are needed. On the other hand, with the expansion of the use of PET imaging devices, the need for drugs for this type of imaging method [fluorodeoxyglucose drug (FDG)] has also increased significantly. FDG is a drug tracer used in the medical imaging technique of PET. The production of FDG requires the production of F-18 and, as a result, reaching O-18 with a richness of more than 95%. There are various methods to produce oxygen with high richness. Among these methods, using a distillation column is a suitable method to produce oxygen, which has low efficiency and high production cost. Optimization of the distillation column can reduce the cost of producing high-rich oxygen. Numerical methods are one of the useful techniques for optimization. In this study, the distillation column has been computerized using mathematical models, and then by changing the number of inputs, including the height of the pipes, the temperature of the input of the distillation column has been optimized. Results show that the maximum separation of the desired isotope concentration in the distillation tower depends on the type of isotope desired and the condition of the device and is independent of the type of feed. Also, the input feed has no effect on the concentration distribution.
引用
收藏
页数:10
相关论文
共 50 条
  • [41] SHELL-MODEL CALCULATION IN 18O
    KOREN, H
    KANESTRO.I
    PHYSICA NORVEGICA, 1968, 3 (02): : 107 - &
  • [42] Dynamic Optimization Study for Cryogenic Distillation in Hydrogen Isotope Separation System
    Urm, Jae Jung
    Park, Damdae
    Choi, Jae Hwan
    Lee, Jae-Uk
    Chang, Min Ho
    Lee, Jong Min
    IFAC PAPERSONLINE, 2022, 55 (07): : 168 - 173
  • [43] Isotope (δD, δ18O) Systematics in Waters of the Russian Arctic Seas
    Dubinina, E. O.
    Kossova, S. A.
    Miroshnikov, A. Yu.
    Kokryatskaya, N. M.
    GEOCHEMISTRY INTERNATIONAL, 2017, 55 (11) : 1022 - 1032
  • [44] Dynamic behavior and control strategy of cryogenic distillation column for hydrogen isotope separation in CFETR
    Wang, Xin
    Chen, Chao
    Li, Jiamao
    Ran, Guangming
    Wang, Heyi
    Xia, Xiulong
    Hou, Jingwei
    Lin, Quansheng
    Xiao, Chengjian
    FUSION ENGINEERING AND DESIGN, 2020, 160
  • [45] Tritium isotope separation by water distillation column packed with silica-gel beads
    Fukada, S
    JOURNAL OF NUCLEAR SCIENCE AND TECHNOLOGY, 2004, 41 (05) : 619 - 623
  • [46] The use of electrolysis for accurate δ17O and δ18O isotope measurements in water
    Meijer, HAJ
    Li, WJ
    ISOTOPES IN ENVIRONMENTAL AND HEALTH STUDIES, 1998, 34 (04) : 349 - 369
  • [47] 18O/16O isotope effect on miscibility of isobutyric acid with water
    Siporska, Agnieszka
    Makowska, Anna
    Szydlowski, Jerzy
    JOURNAL OF PHYSICAL CHEMISTRY B, 2007, 111 (40): : 11632 - 11634
  • [48] KINETIC FRACTIONATION OF THE ISOTOPE COMPOSITION OF 18O, 13C, AND OF CLUMPED ISOTOPE 18O13C IN CALCITE DEPOSITED TO SPELEOTHEMS. IMPLICATIONS TO THE RELIABILITY OF THE 18O AND Δ47- PALEOTHERMOMETERS
    Dreybrodt, Wolfgang
    ACTA CARSOLOGICA, 2019, 48 (03) : 329 - 340
  • [49] VARIABLE STAGE-NUMBER MODEL FOR SIMULATING BATCH OPERATION OF WATER DISTILLATION COLUMN FOR TRITIUM ISOTOPE-SEPARATION
    KABA, A
    YAMAMOTO, I
    KANAGAWA, A
    JOURNAL OF NUCLEAR SCIENCE AND TECHNOLOGY, 1988, 25 (07) : 586 - 593
  • [50] MATHEMATICAL-MODEL FOR SIMULATING SEPARATION OF MULTICOMPONENT MIXTURES BY DISTILLATION
    KIRBACH, V
    FRENZEL, L
    STRANKMU.H
    CHEMISCHE TECHNIK, 1973, 25 (12): : 721 - 722