• 文献检索
  • 文档翻译
  • 深度研究
  • 学术资讯
  • Suppr Zotero 插件Zotero 插件
  • 邀请有礼
  • 套餐&价格
  • 历史记录
应用&插件
Suppr Zotero 插件Zotero 插件浏览器插件Mac 客户端Windows 客户端微信小程序
定价
高级版会员购买积分包购买API积分包
服务
文献检索文档翻译深度研究API 文档MCP 服务
关于我们
关于 Suppr公司介绍联系我们用户协议隐私条款
关注我们

Suppr 超能文献

核心技术专利:CN118964589B侵权必究
粤ICP备2023148730 号-1Suppr @ 2026

文献检索

告别复杂PubMed语法,用中文像聊天一样搜索,搜遍4000万医学文献。AI智能推荐,让科研检索更轻松。

立即免费搜索

文件翻译

保留排版,准确专业,支持PDF/Word/PPT等文件格式,支持 12+语言互译。

免费翻译文档

深度研究

AI帮你快速写综述,25分钟生成高质量综述,智能提取关键信息,辅助科研写作。

立即免费体验

基于膜的脱盐过程中驱动压力之间数学关系的理论分析

Theoretical Analysis of a Mathematical Relation between Driving Pressures in Membrane-Based Desalting Processes.

作者信息

Chae Sung Ho, Kim Joon Ha

机构信息

School of Earth Sciences and Environmental Engineering, Gwangju Institute of Science and Technology (GIST), Gwangju 61005, Korea.

International Environmental Research Institute, Gwangju Institute of Science and Technology (GIST), Gwangju 61005, Korea.

出版信息

Membranes (Basel). 2021 Mar 19;11(3):220. doi: 10.3390/membranes11030220.

DOI:10.3390/membranes11030220
PMID:33808923
原文链接:https://pmc.ncbi.nlm.nih.gov/articles/PMC8003649/
Abstract

Osmotic and hydraulic pressures are both indispensable for operating membrane-based desalting processes, such as forward osmosis (FO), pressure-retarded osmosis (PRO), and reverse osmosis (RO). However, a clear relation between these driving pressures has not thus far been identified; hence, the effect of change in driving pressures on systems has not yet been sufficiently analyzed. In this context, this study formulates an actual mathematical relation between the driving pressures of membrane-based desalting processes by taking into consideration the presence of energy loss in each driving pressure. To do so, this study defines the pseudo-driving pressures representing the water transport direction of a system and the similarity coefficients that quantify the energy conservation rule. Consequently, this study finds three other theoretical constraints that are required to operate membrane-based desalting processes. Furthermore, along with the features of the similarity coefficients, this study diagnoses the commercial advantage of RO over FO/PRO and suggests desirable optimization sequences applicable to each process. Since this study provides researchers with guidelines regarding optimization sequences between membrane parameters and operational parameters for membrane-based desalting processes, it is expected that detailed optimization strategies for the processes could be established.

摘要

渗透压和液压对于诸如正向渗透(FO)、压力延迟渗透(PRO)和反渗透(RO)等基于膜的脱盐过程的运行都是不可或缺的。然而,到目前为止,尚未确定这些驱动压力之间的明确关系;因此,驱动压力变化对系统的影响尚未得到充分分析。在此背景下,本研究通过考虑每个驱动压力中能量损失的存在,建立了基于膜的脱盐过程驱动压力之间的实际数学关系。为此,本研究定义了表示系统水传输方向的伪驱动压力和量化能量守恒规则的相似系数。因此,本研究发现了基于膜的脱盐过程运行所需的另外三个理论约束条件。此外,结合相似系数的特点,本研究分析了反渗透相对于正向渗透/压力延迟渗透的商业优势,并提出了适用于每个过程的理想优化顺序。由于本研究为研究人员提供了基于膜的脱盐过程中膜参数和操作参数之间优化顺序的指导方针,预计可以建立该过程的详细优化策略。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9aa5/8003649/be7362abe408/membranes-11-00220-g009.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9aa5/8003649/99889a4e7a7a/membranes-11-00220-g001.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9aa5/8003649/7cf68ec8859f/membranes-11-00220-g002.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9aa5/8003649/3ed26217626f/membranes-11-00220-g003.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9aa5/8003649/6040cbad1c9d/membranes-11-00220-g004.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9aa5/8003649/d9b874fc9366/membranes-11-00220-g005.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9aa5/8003649/b34c2966fbf7/membranes-11-00220-g006.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9aa5/8003649/a226eca75b14/membranes-11-00220-g007.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9aa5/8003649/70abcaabe1c2/membranes-11-00220-g008.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9aa5/8003649/be7362abe408/membranes-11-00220-g009.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9aa5/8003649/99889a4e7a7a/membranes-11-00220-g001.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9aa5/8003649/7cf68ec8859f/membranes-11-00220-g002.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9aa5/8003649/3ed26217626f/membranes-11-00220-g003.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9aa5/8003649/6040cbad1c9d/membranes-11-00220-g004.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9aa5/8003649/d9b874fc9366/membranes-11-00220-g005.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9aa5/8003649/b34c2966fbf7/membranes-11-00220-g006.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9aa5/8003649/a226eca75b14/membranes-11-00220-g007.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9aa5/8003649/70abcaabe1c2/membranes-11-00220-g008.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9aa5/8003649/be7362abe408/membranes-11-00220-g009.jpg

相似文献

1
Theoretical Analysis of a Mathematical Relation between Driving Pressures in Membrane-Based Desalting Processes.基于膜的脱盐过程中驱动压力之间数学关系的理论分析
Membranes (Basel). 2021 Mar 19;11(3):220. doi: 10.3390/membranes11030220.
2
Forward Osmosis Membranes under Null-Pressure Condition: Do Hydraulic and Osmotic Pressures Have Identical Nature?零压条件下的正向渗透膜:水力压力和渗透压具有相同的本质吗?
Environ Sci Technol. 2018 Mar 20;52(6):3556-3566. doi: 10.1021/acs.est.7b05265. Epub 2018 Mar 1.
3
Pressure retarded osmosis for energy production: membrane materials and operating conditions.压力延缓渗透用于能源生产:膜材料和操作条件。
Water Sci Technol. 2012;65(10):1789-94. doi: 10.2166/wst.2012.025.
4
Adverse impact of feed channel spacers on the performance of pressure retarded osmosis.进料通道隔垫对压力延迟渗透性能的不利影响。
Environ Sci Technol. 2012 Apr 17;46(8):4673-81. doi: 10.1021/es3002597. Epub 2012 Mar 28.
5
What governs the nature of fouling in forward osmosis (FO) and reverse osmosis (RO)? A molecular dynamics study.是什么控制着正向渗透(FO)和反渗透(RO)中的污染性质?一项分子动力学研究。
Phys Chem Chem Phys. 2019 Nov 7;21(43):24165-24176. doi: 10.1039/c9cp04393d.
6
Application of volume-retarded osmosis and low-pressure membrane hybrid process for water reclamation.体积延迟渗透与低压膜混合工艺在水回收中的应用。
Chemosphere. 2018 Mar;194:76-84. doi: 10.1016/j.chemosphere.2017.11.067. Epub 2017 Nov 15.
7
Unlocking High-Salinity Desalination with Cascading Osmotically Mediated Reverse Osmosis: Energy and Operating Pressure Analysis.级联渗透压介导反渗透法实现高盐度海水淡化:能量和操作压力分析。
Environ Sci Technol. 2018 Feb 20;52(4):2242-2250. doi: 10.1021/acs.est.7b05774. Epub 2018 Feb 7.
8
Fouling propensity of novel TFC membranes with different osmotic and hydraulic pressure driving forces.不同渗透和水力压力驱动力下新型 TFC 膜的污染倾向。
Water Res. 2020 May 15;175:115657. doi: 10.1016/j.watres.2020.115657. Epub 2020 Feb 28.
9
The use of ultrasound to reduce internal concentration polarization in forward osmosis.利用超声减少正向渗透中的内部浓差极化。
Ultrason Sonochem. 2018 Mar;41:475-483. doi: 10.1016/j.ultsonch.2017.10.005. Epub 2017 Oct 5.
10
Application of forward osmosis technology in crude glycerol fermentation biorefinery-potential and challenges.正向渗透技术在粗甘油发酵生物炼制厂中的应用——潜力与挑战。
Bioprocess Biosyst Eng. 2018 Aug;41(8):1089-1101. doi: 10.1007/s00449-018-1938-8. Epub 2018 Apr 24.

引用本文的文献

1
Numerical Modeling in Membrane Processes.膜过程中的数值模拟
Membranes (Basel). 2022 Oct 23;12(11):1030. doi: 10.3390/membranes12111030.

本文引用的文献

1
On the understanding and feasibility of "Breakthrough" Osmosis.关于“突破”渗透的理解和可行性。
Sci Rep. 2019 Nov 11;9(1):16464. doi: 10.1038/s41598-019-53417-6.
2
Evidence, Determination, and Implications of Membrane-Independent Limiting Flux in Forward Osmosis Systems.证据、确定和膜独立限制通量在正向渗透系统中的意义。
Environ Sci Technol. 2019 Apr 16;53(8):4380-4388. doi: 10.1021/acs.est.8b05925. Epub 2019 Apr 1.
3
Forward Osmosis Membranes under Null-Pressure Condition: Do Hydraulic and Osmotic Pressures Have Identical Nature?
零压条件下的正向渗透膜:水力压力和渗透压具有相同的本质吗?
Environ Sci Technol. 2018 Mar 20;52(6):3556-3566. doi: 10.1021/acs.est.7b05265. Epub 2018 Mar 1.
4
Osmosis is not driven by water dilution.渗透作用不是由水稀释驱动的。
Trends Plant Sci. 2013 Apr;18(4):195-7. doi: 10.1016/j.tplants.2012.12.001. Epub 2013 Jan 5.
5
Thin-film composite pressure retarded osmosis membranes for sustainable power generation from salinity gradients.用于从盐度梯度中可持续发电的薄膜复合压力延迟渗透膜。
Environ Sci Technol. 2011 May 15;45(10):4360-9. doi: 10.1021/es104325z. Epub 2011 Apr 14.
6
Thermodynamic analysis of the permeability of biological membranes to non-electrolytes.生物膜对非电解质渗透性的热力学分析
Biochim Biophys Acta. 1958 Feb;27(2):229-46. doi: 10.1016/0006-3002(58)90330-5.