Foam drainage with twin inputs in two dimensions
文献类型：期刊论文
| 作者 | Huang, Jin; Sun, Qicheng |
| 刊名 | COLLOIDS AND SURFACES A-PHYSICOCHEMICAL AND ENGINEERING ASPECTS
 |
| 出版日期 | 2007-11-01 |
| 卷号 | 309期号:1-3页码:132-136 |
| 关键词 | foam drainage twin inputs experiment simulation |
| ISSN号 | 0927-7757 |
| 其他题名 | Colloid Surf. A-Physicochem. Eng. Asp. |
| 中文摘要 | Forced foam drainage is the flow of constantly input liquid through the network of interstitial channels between bubbles in foam under actions of gravity and capillarity. When two streams of liquid are input with twin narrow nozzles separated with a distance, they usually merge into a singular drainage wave to propagate in foams. This work reports results of behaviours of the merged drainage wave. We find that (1) along the vertical direction beneath one nozzle, the liquid spreading is well described by power law with exponents greater than that of individual drainage. (2) Along the vertical direction down the center of the two nozzles, we find the spreading speed is nearly constant for a fixed separation. As the separation distance increases six times, the speed increases only about 14%. This result would benefit designing of micro-mixers and niicro-reactors, based on foam-like channels, for liquid/liquid systems widely used in pharmaceutical industry. (c) 2007 Elsevier B.V. All rights reserved. |
| 英文摘要 | Forced foam drainage is the flow of constantly input liquid through the network of interstitial channels between bubbles in foam under actions of gravity and capillarity. When two streams of liquid are input with twin narrow nozzles separated with a distance, they usually merge into a singular drainage wave to propagate in foams. This work reports results of behaviours of the merged drainage wave. We find that (1) along the vertical direction beneath one nozzle, the liquid spreading is well described by power law with exponents greater than that of individual drainage. (2) Along the vertical direction down the center of the two nozzles, we find the spreading speed is nearly constant for a fixed separation. As the separation distance increases six times, the speed increases only about 14%. This result would benefit designing of micro-mixers and niicro-reactors, based on foam-like channels, for liquid/liquid systems widely used in pharmaceutical industry. (c) 2007 Elsevier B.V. All rights reserved. |
| WOS标题词 | Science & Technology ; Physical Sciences |
| 类目[WOS] | Chemistry, Physical |
| 研究领域[WOS] | Chemistry |
| 关键词[WOS] | AQUEOUS FOAMS ; 2 DIMENSIONS ; EQUATION ; FLOW |
| 收录类别 | ISTP ; SCI |
| 原文出处 | |
| 语种 | 英语 |
| WOS记录号 | WOS:000250191600019 |
| 公开日期 | 2013-10-15 |
| 版本 | 出版稿 |
| 源URL | [http://ir.ipe.ac.cn/handle/122111/3342]  |
| 专题 | 过程工程研究所_研究所（批量导入） |
| 作者单位 | Chinese Acad Sci, Inst Proc Engn, Beijing, Peoples R China |
| 推荐引用方式 GB/T 7714 | Huang, Jin,Sun, Qicheng. Foam drainage with twin inputs in two dimensions[J]. COLLOIDS AND SURFACES A-PHYSICOCHEMICAL AND ENGINEERING ASPECTS,2007,309(1-3):132-136. |
| APA | Huang, Jin,&Sun, Qicheng.(2007).Foam drainage with twin inputs in two dimensions.COLLOIDS AND SURFACES A-PHYSICOCHEMICAL AND ENGINEERING ASPECTS,309(1-3),132-136. |
| MLA | Huang, Jin,et al."Foam drainage with twin inputs in two dimensions".COLLOIDS AND SURFACES A-PHYSICOCHEMICAL AND ENGINEERING ASPECTS 309.1-3(2007):132-136. |
入库方式： OAI收割
来源：过程工程研究所
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