Yu. 2009. On the Physical Properties of Apparent Two Phase Fractal Porous Media

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第八届国际凝聚态理论与计算材料学会议

第八届国际凝聚态理论与计算材料学会议

大会将请专家对以下领域作专题性的特邀报告:
(1). 凝聚态物理的最新进展:
A. 自旋电子学
B. 纳米材料
C. 固体量子信息和计算
D. 玻色-爱因斯坦凝聚
E. 强关联电子系统
F. 高温超导
G. 量子霍尔效应
H. 磁学
I 表面和界面
J. 半导体物理
K. 低维凝聚态物理
L. 介观物理
M. 软凝聚态物质
N. 生物物理
structure Metallic Phases in Solid Germane (GeH4) under Pressure 锗烷在
压力下的金属相
11:45 -12:15
12:15 -13:00
午餐
张振宇 橡树岭国家实验室
柳百新
清华大学
林海青 香港中文大学 牛谦 美国德克萨斯大学
7 月 16 日
凝聚态理论专题邀请报告 I 主持人:谢心澄 地点:芙蓉厅
14:30 -14:55 14:55 -15:20 15:20 -15:45 15:45 -16:10 16:10 -16:35 16:35 -16:50
7 月 16 日
Manipulating Magnetization States of Nanostructures Two-spin decoherence in semiconductor quantum dots
稀磁半导体(Al,Cr)N 中的氮空位与高温铁磁性的第一原理研究
蒋青 刘邦贵
吉林大学 中科院物理所
15:20 -15:45 15:45 -16:10 16:10 -16:35
Theoretical and experimental studies of semiconductor dilute nitrides and devices

页岩油储层压裂–提采一体化研究进展与面临的挑战

页岩油储层压裂–提采一体化研究进展与面临的挑战

◄油气开发►doi:10.11911/syztjs.2024012引用格式:张衍君,王鲁瑀,刘娅菲,等. 页岩油储层压裂–提采一体化研究进展与面临的挑战[J]. 石油钻探技术,2024, 52(1):84-95.ZHANG Yanjun, WANG Luyu, LIU Yafei, et al. Advances and challenges of integration of fracturing and enhanced oil recovery in shale oil reservoirs [J]. Petroleum Drilling Techniques ,2024, 52(1):84-95.页岩油储层压裂–提采一体化研究进展与面临的挑战张衍君1, 王鲁瑀2, 刘娅菲1, 张佳亮3, 周德胜1, 葛洪魁3(1. 西安石油大学石油工程学院, 陕西西安 710065;2. 香港理工大学土木及环境工程系, 香港 999077;3. 中国石油大学(北京)非常规油气科学技术研究院, 北京 102249)摘 要: 页岩油储层压裂开发中,以远超地层吸收能力的注入速率向储层注入包含各类添加剂的工作液,基本完成了压裂介质一次注入、油井开发全生命周期受益的使命。

其中,2个问题尤为关键:1)如何形成均匀展布的裂缝网络,增大裂缝和储层的接触面积、提高液体流动效率?2)在形成高效传压传质缝网的基础上,存地压裂液如何提高储层中原油的可动性?压裂和提采一体化是解决上述问题的重要思路。

为此,阐述了页岩油储层压裂–提采一体化的内涵,归纳了实现压裂–提采一体化的模拟和试验技术;明确了页岩油储层压裂–提采一体化的科学问题:均衡应力压裂形成均匀展布的缝网,提高均布缝网中流体流动与传输的效率,强化基质孔隙中油气的动用。

同时,指出了压裂–提采一体化面临的挑战:明确裂缝非均匀扩展导致的压裂井间干扰机理并建立控制方法,形成裂缝中高压流体高效作用于基质孔隙的途径,揭示压裂液–储层–原油相互作用提高原油可动性机理。

多孔介质孔道网络模型与等温干燥模拟

多孔介质孔道网络模型与等温干燥模拟

N(0.8944,0.14952)
77
3.2 干燥机理分析
侵入渗流的概念最先由Willemsen和Wilkinson提出[12,23],主要应用于多孔介质两相及多 相流研究。侵入渗流的机理基于不溶混置换理论的毛细指进,认为毛细压力在多孔介质内部 流体流动中起主要作用,侵入流体首先突破毛细压力阈值最小的孔道。假设干燥过程缓慢, 干空气流速较小,并忽略水、空气等流体粘度的影响,则可将干燥过程比拟为侵入渗流过程。 但两者又不完全相同:侵入渗流过程没有蒸发,而干燥过程存在蒸发现象。在干燥中,液态 水逐渐蒸发,水蒸气沿着内部孔道向外扩散。砂床孔隙较大,因此忽略开尔文效应的影响。
对于孔道节点(i,j-1)和(i,j-2)之间的喉道的蒸气质量传递计算我们可以以此类推。
且模型边界处蒸发面上喉道的蒸气质量流率 q 为:
q = π d 2 hM (C1 j − C ∞ ) 4 (1 + β ) a / 2
(10)
式中:C∞为干燥介质(环境空气)中水蒸气的浓度。
在每个气相节点处,应有湿分质量平衡:
0 引言
多孔介质是指“带有孔洞的固体”,在自然界中普遍存在,土壤、岩石、各种农业物料 等等都属于多孔介质。作为干燥对象的固体物料,大部分是多孔介质。长期以来,人们对多 孔介质干燥展开了许多研究,但直到如今,由于多孔介质干燥过程复杂,其干燥机理仍未研 究透彻[1-4]。
常用的多孔介质干燥理论,如液态扩散理论,蒸发-凝结理论,Luikov理论,Whitaker 体积平均理论等[5-8]都基于连续体假设,即将多孔介质假想为虚拟的连续体。而事实上,多 孔介质内部结构复杂,在大部分情况下更接近于离散体。因此,这类理论本身存在一定不足, 如干燥中的干、湿斑和恒速干燥阶段等现象,就无法用连续体假设理论解释[8, 9]。上世纪 90 年代初,Daian、Nowicki等人将渗流研究中的孔道网络方法引入多孔介质干燥研究中,后经 Prat和Yortsos等人的发展,逐渐形成了孔道网络干燥理论[10-17]。这一理论认为被湿分在物料 中不均匀分布,采用节点及与其相互连接的孔道来描述多孔介质内部的拓扑结构,在孔道等 级上研究多孔介质的热质传递。

扫描电镜下断口表面的三维重建及分形维数的测量_王怀文

扫描电镜下断口表面的三维重建及分形维数的测量_王怀文

第23卷第2期2008年4月实验力学JO U RN A L OF EX PERIM EN T A L M ECH A N ICSV o l.23No.2A pr.2008文章编号:1001-4888(2008)02-0118-07扫描电镜下断口表面的三维重建及分形维数的测量*王怀文1,周宏伟1,谢和平1,2,左建平1,李艳杰1(1.中国矿业大学(北京)岩石力学与分形研究所,北京100083;2.四川大学,成都610065)摘要:基于数字散斑相关方法,利用扫描电镜立体对技术和计算机视觉方法实现了物体表面的三维重建,讨论了影响其精度的原因,并且利用分形理论对表面的三维形貌进行了定量分析,由立方体覆盖法得到了三维形貌的分形维数。

作为应用的实例,将该方法应用到岩石断口的三维重建中,得到了重建后的高度云图和分形维数。

结果表明,利用扫描电镜立体对技术对断口表面进行三维重构并进行分形维数的计算是一种行之有效的断口定量分析方法。

这为研究材料断裂的微观机理、断裂过程和断裂性质等问题提供了一种途径。

关键词:扫描电镜;三维重建;分形维数;数字相关方法中图分类号:O348文献标识码:A0引言三维重建是计算机视觉领域中的一个重要研究方向,主要是由两幅或者多幅两维图像恢复物体的三维几何形貌。

目前由两个普通摄像机分别获取的两维图像进行三维重建的技术已经比较成熟[1],扫描电镜下的三维重建也在20世纪90年代开始起步并得到发展[2,3]。

由于SEM具有分辨率高、景深大和可以直接观察试样等特点,特别适合于对断口进行分析研究,从而使显微断口SEM成像技术成为一种广泛用于研究断裂的方法。

但是,扫描电镜的成像技术是将立体的景物经过透视投影在二维平面上,损失了景物的深度信息,这给断口图像的平面分析带来很大的局限性。

为了得到断口图像完整的三维信息,在SEM下进行断口的三维重建具有较大的实用性。

定量的断口分析可以为揭示断裂微观机理、断裂过程和断裂性质等问题提供可靠的依据,从而更好地研究材料和零部件的失效。

高煤阶煤孔隙结构及分形特征

高煤阶煤孔隙结构及分形特征

高煤阶煤孔隙结构及分形特征李振;邵龙义;侯海海;郭双庆;赵升;姚铭檑;阎纯忠【摘要】高煤阶煤与中低煤阶煤在孔隙结构特征方面存在明显差异,分形理论为定量描述高煤阶煤储层孔隙特征提供了有效手段.基于扫描电镜、压汞实验和孔渗测试,以华北地区最大镜质体反射率(R0.max)在1.9%~2.95%之间的9个煤样为研究对象,采用分段回归的方法对各样品进行不同孔径段分形维数计算,并讨论了孔隙结构分形维数与孔隙体积百分比、Ro,max、孔隙度和渗透率的关系.结果表明,高煤阶煤微小孔发育,半封闭孔含量较高,孔隙连通性一般,且孔隙结构具有明显的分段分形特征,同一煤样的超大孔(孔隙半径r>5 μm)、大孔(0.5 μm<r<5 μm)、中孔(0.05μm<r<0.5μm)和微小孔(r <0.05 tμm)的分形维数依次减小;各煤样超大孔、大孔、中孔分形维数均随Ro.max增加而增加,随对应孔隙体积百分比增加而减小;孔隙度或渗透率与超大孔、大孔和中孔、微小孔分形维数分别呈二次相关、线性正相关、负相关;各分形区间分形维数分布的偏度和峰度与孔隙度或渗透率分别呈高度正相关和负相关,这为高煤阶煤孔隙度、渗透率提供了理想的线性方程(y=ax+b)预测模型.%Significant differences exist in pore structures between highrank coals and medium-low rank coals,and the principle of fractal geometry is an effective tool for quantitatively describing pore characteristics of high rank coal reservoirs.The experiments comprising scanning electron microscopy,mercury intrusion,porosity and permeability testing were performed on nine coal samples (R from 1.9% to 2.95%) from North China.The pore fractal dimensions of samples were calculated using the subsection regression method and the relationships between the pore fractal dimension and different parameters including pore volumepercent,coal degree of metamorphism,porosity and permeability were discussed.The results show that coal samples are characterized by abundant micro-ascopores,relatively high semi-closed porecontent,general pore connectivity and clearly piecewise fractal dimensions.For each sample,fractal dimensions of supermacropore (pore radius r >5 μm),macropore (0.5 μm < r <5 μm),mesopore (0.05 μm < r <0.5 μm) and micro-ascopore (r <0.05 μm) decrease in turn.In addition,fractal dimensions of these pores except micro-ascopores increase with the increasing R and decreasing pore volume percent for all samples.The correlations between coal porosity (or permeability) and fractal dimensions of supermacropore,macropore and mesopore,micro-ascopore present as quadratic,linearly positive and linearly negative curves,respectively.The skewness and kurtosis of fractal dimension distribution for each sample are positively and negatively associated with porosity or permeability respectively.Meanwhile,based on skewness and kurtosis,the prediction models of linear equations (y =ax + b) can be used to predict porosity and permeability of high rank coals.【期刊名称】《现代地质》【年(卷),期】2017(031)003【总页数】11页(P595-605)【关键词】高煤阶煤;孔隙结构;分形维数;压汞实验【作者】李振;邵龙义;侯海海;郭双庆;赵升;姚铭檑;阎纯忠【作者单位】中国矿业大学(北京)地球科学与测绘工程学院,北京100083;中国矿业大学(北京)地球科学与测绘工程学院,北京100083;中国矿业大学(北京)地球科学与测绘工程学院,北京100083;河南省煤田地质局三队,河南郑州450046;中国矿业大学(北京)地球科学与测绘工程学院,北京100083;中国矿业大学(北京)地球科学与测绘工程学院,北京100083;河南省煤田地质局三队,河南郑州450046【正文语种】中文【中图分类】P618.11;TE122.2煤储层具有复杂的孔裂隙系统和很强的非均质性[1-2],同时煤中的孔裂隙系统跨越的空间尺度大,影响着煤中气体的吸附和运移[3-5]。

材料类期刊投稿指南

材料类期刊投稿指南

材料类期刊投稿指南SCI(EI)收录的科技期刊(2003)1 NATURE NATURE 自然0028-0836 27.955/2 SCIENCE SCIENCE 科学0036-8075 23.329/3 SURF SCI REP SURFACE SCIENCE REPORTS 表面科学报告0167-5729 14.091/science/journal/016757294 PROG MATER SCI PROGRESS IN MATERIALS SCIENCE 材料科学进展0079-6425 14http//www.elsevier.nl/inca/publications/store/4/1/4/5 PROG SURF SCI PROGRESS IN SURFACE SCIENCE 表面科学进展0079-6816 7.96/science/journal/007968166 PHYS REV LETT PHYSICAL REVIEW LETTERS 物理评论快报0031-9007 6.668 /7 MAT SCI ENG R MATERIALS SCIENCE & ENGINEERING R-REPORTS 材料科学与工程报告0927-796X 6.143/science/journal/0927796X8 ADV POLYM SCI ADVANCES IN POLYMER SCIENCE 聚合物科学发展0065-3195 6.053/science/journal/007967009 ADV MATER ADVANCED MATERIALS 先进材料0935-9648 5.579http://www.wiley-vch.de/publish/en/journals/alphabeticIndex/2089/10 ANNU REV MATER SCI ANNUAL REVIEW OF MATERIALS SCIENCE 材料科学年度评论0084-6600 5.405/loi/matsci?cookieSet=111 APPL PHYS LETT APPLIED PHYSICS LETTERS 应用物理快报0003-6951 3.849 /aplo/12 PROG POLYM SCI PROGRESS IN POLYMER SCIENCE 聚合物科学进展0079-6700 3.738/science/journal/0079670013 CHEM MATER CHEMISTRY OF MATERIALS 材料化学0897-4756 3.69/journals/cmatex/14 PHYS REV B PHYSICAL REVIEW B 物理评论B 0163-1829 3.07/15 ADV CHEM PHYS ADVANCES IN CHEMICAL PHYSICS 物理化学发展0065-2385 2.828/WileyCDA/WileyTitle/productCd-0471214531.html16 J MATER CHEM JOURNAL OF MATERIALS CHEMISTRY 材料化学杂志0959-9428 2.736/is/journals/current/jmc/mappub.htm17 ACTA MATER ACTA MATERIALIA 材料学报1359-6454 2.658 http://www.elsevier.nl/locate/actamat/18 MRS BULL MRS BULLETIN 材料研究学会(美国)公告0883-7694 2.606/publications/bulletin/19 BIOMATERIALS BIOMATERIALS 生物材料0142-9612 2.489 /20 CARBON CARBON 碳0008-6223 2.34/inca/publications/store/2/5/8/21 SURF SCI SURFACE SCIENCE 表面科学0039-6028 2.189/science/journal/0169433222 J APPL PHYS JOURNAL OF APPLIED PHYSICS 应用物理杂志0021-8979 2.128 /japo/23 CHEM VAPOR DEPOS CHEMICAL VAPOR DEPOSITION 化学气相沉积0948-1907 2.123http://www.wiley-vch.de/publish/dt/24 J BIOMED MATER RES JOURNAL OF BIOMEDICAL MATERIALS RESEARCH 生物医学材料研究0021-9304 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/science/journal/14666049174 SCI TECHNOL WELD JOI SCIENCE AND TECHNOLOGY OF WELDING AND JOINING 焊接科学与技术1362-1718 0.295 /phase-trans/abstracts/stwj.html175 MATER MANUF PROCESS MATERIALS AND MANUFACTURING PROCESSES 材料与制造工艺1042-6914 0.288 /servlet/product/productid/AMP176 FERROELECTRICS LETT FERROELECTRICS LETTERS SECTION 铁电材料快报0731-5171 0.274 /journals/titles/07315171.html177 J MATER SCI TECHNOL JOURNAL OF MATERIALS SCIENCE & TECHNOLOGY 材料科学与技术杂志1005-0302 0.269 http://coral.dir.bg/jmst-h.htm178 J MATER ENG PERFORM JOURNAL OF MATERIALS ENGINEERING AND PERFORMANCE 材料工程与性能杂志1059-9495 0.268 /science/journal/10599495179 MET MATER-INT METALS AND MATERIALS INTERNATIONAL 国际金属及材料1225-9438 0.256 http://www.icm.re.kr/doc/paper/index.jsp?flag=kor&jcode=499180 GLASS TECHNOL GLASS TECHNOLOGY 玻璃技术0017-1050 0.255 http://www.societyof /181 J MATER PROCESS TECH JOURNAL OF MATERIALS PROCESSING TECHNOLOGY 材料加工技术杂志0924-0136 0.255 /science/journal/09240136182 J POLYM MATER JOURNAL OF POLYMER MATERIALS 聚合物材料杂志0970-0838 0.229http://balkema.ima.nl/scripts/cgiBalkema.exe/serie?SerNo=40183 ADV POWDER TECHNOL ADVANCED POWDER TECHNOLOGY 先进粉末技术0921-8831 0.224 /journals/jn-AdvPowTec.html184 J ADV MATER JOURNAL OF ADVANCED MATERIALS 先进材料杂志1070-9789 0.22/JAM.html185 SYNTHESE SYNTHESE 合成0039-7857 0.208/issn/0039-7857186 GLASS SCI TECHNOL GLASS SCIENCE AND TECHNOLOGY-GLASTECHNISCHE BERICHTE 玻璃科学与技术0946-7475 0.189/isi/187 J TEST EVAL JOURNAL OF TESTING AND EVALUATION 测试及评价杂志0090-3973 0.171/cgi-bin/SoftCart.exe/index.shtml?E+mystore188 MATER SCI TECH-LOND MATERIALS SCIENCE AND TECHNOLOGY 材料科学与技术0267-0836 0.171 /~tw/home.html189 POWDER METALL MET C+ POWDER METALLURGY AND METAL CERAMICS 粉末冶金及金属陶瓷1068-1302 0.161 /issn/1068-1302/contents190 MATER SCI+ MATERIALS SCIENCE 材料科学1068-820X 0.15 /191 MATER TECHNOL MATERIALS TECHNOLOGY 材料技术1066-7857 0.147/192 ADV MATER PROCESS ADVANCED MATERIALS & PROCESSES 先进材料及工艺0882-7958 0.144 /193 RARE METALS RARE METALS 稀有金属1001-0521 0.142 / 194 J WUHAN UNIV TECHNOL JOURNAL OF WUHAN UNIVERSITY OF TECHNOLOGY-MATERIALS SCIENCE EDITION 武汉理工大学学报-材料科学版1000-2413 0.14/journal/english/order.htm195 PLAT SURF FINISH PLATING AND SURFACE FINISHING 电镀和表面修整0360-3164 0.14/196 J INORG MATER JOURNAL OF INORGANIC MATERIALS 无机材料杂志1000-324X 0.131/science/journal/14666049197 MATER WORLD MATERIALS WORLD 材料世界0967-8638 0.104 /198 MET SCI HEAT TREAT+ METAL SCIENCE AND HEAT TREATMENT 金属科学及热处理0026-0673 0.096 /issn/0026-0673/current199 METALL METALL 金属0026-0746 0.096 http://www.vsb.cz/200 MATER PERFORMANCE MATERIALS PERFORMANCE 材料性能0094-1492 0.087/nace/content/publications/mediakit.asp#MP201 J MATER PROCESS MANU JOURNAL OF MATERIALS PROCESSING & MANUFACTURING SCIENCE 材料加工与制造科学杂志1062-0656 0.078 /journal.aspx?pid=316202 SCI ENG COMPOS MATER SCIENCE AND ENGINEERING OF COMPOSITE MATERIALS 复合材料科学与工程0334-181X 0.075/exec/obidos/ASIN/B00006KWDC/shoppingsavvy-20/002-4085689-4536025203 IEEE T COMPON PACK T IEEE TRANSACTIONS ON COMPONENTS AND PACKAGING TECHNOLOGIES IEEE元件及封装技术会刊1521-3331 0.071/xpl/RecentIssue.jsp?puNumber=6144204 JOCCA-SURF COAT INT JOCCA-SURFACE COATINGS INTERNATIONAL JOCCA—国际表面涂层1356-0751 /publications/sci/sci_sso205 ADV FUNCT MATER ADVANCED FUNCTIONAL MATERIALS 先进功能材料1616-301X/cgi-bin/jhome/77003362?CRETRY=1206 ANN REV MATER RES ANNUAL REVIEW OF MATERIALS RESEARCH 材料研究年度评论1531-7331 /loi/matsci207 MATER TRANS MATERIALS TRANSACTIONS 材料会刊1345-9678/pubs/journals/MT/MT.html。

活性炭英文描述

活性炭英文描述

Product Description:our company's product nut shell activated carbon is a nonpolar adsorben,it selects high quality shells and anthracite as the raw material, through the processing, dehydration,carbonization, Our facotry is certified by ISO9001:2000,ISO9001-2008.activation , processed from the use of advanced technology refined.Appearance is black powder, granules, column and so on .Significant advantages:1)high developed porous structure;2)large specifiction surface area;3)adsorption capacity;4)high mechanical intensity;5)renewable etc.Function:widely used in toxic gas purification, waste gas treatment,agriculture environment protection,national defense industrial, industrial and water purification processing the solvent recovery etc.Amount of Use: According to the different water quality, it is depends on production process.Quality Index:(HG3-1290-80)Item Test Data Item Test DataGranularity diameter 0.4-3mm Real specific gravity 2-2.2g/cm3Phenol adsorption rate 450mg/g bulk specific weight 0.45-0.55g/cm3 Hardness ≥80-95% Total porous volume 0.7-1cm3/gIodine number 1000-1100mg/g Specific surface area 590-1500m2/g Methylene blue number 100-150mg/g PH value 8-10Half de-chlorine value ≤5cm Ash ≤8-12%Moisture ≤3%Specific heat -1.00J/g. °CActivated carbonFrom Wikipedia, the free encyclopedia(Redirected from Active carbon)This article may be divided into too many sections considering its overall length. Tohelp improve Wikipedia's quality standards, some of the sections may need to becondensed or merged. Please discuss this issue on the talk page. October 2009Activated carbonActivated carbon, also called activated charcoal or activated coal is a form of carbon that has been processed to make it extremely porous and thus to have a very large surface area available for adsorption or chemical reactions.[1]The word activated in the name is sometimes replaced with active. Due to its high degree of microporosity, just 1 gram of activated carbon has a surface area in excess of 500 m2 (about one tenth the size of a football field), as determined typically by nitrogen gas adsorption. Sufficient activation for useful applications may come solely from the high surface area, though further chemical treatment often enhances the absorbing properties of the material. Activated carbon is usually derived from charcoal.ProductionActivated carbon is carbon produced from carbonaceous source materials like nutshells, peat, wood, coir, lignite, coal and petroleum pitch. It can be produced by one of the following processes:1Physical reactivation: The precursor is developed into activated carbons using gases.This is generally done by using one or a combination of the following processes:▪Carbonization: Material with carbon content is pyrolyzed at temperatures in therange 600–900 °C, in absence of oxygen (usually in inert atmosphere with gases likeargon or nitrogen)▪Activation/Oxidation: Raw material or carbonized material is exposed tooxidizing atmospheres (carbon monoxide, oxygen, or steam) at temperatures above250 °C, usually in the temperature range of 600–1200 °C.2Chemical activation: Prior to carbonization, the raw material is impregnated with certain chemicals. The chemical is typically an acid, strong base, or a salt(phosphoric acid, potassium hydroxide, sodium hydroxide, zinc chloride, respectively). Then, the raw material is carbonized at lower temperatures (450–900 °C). It is believed that the carbonization / activation step proceeds simultaneously with the chemical activation. Chemical activation is preferred over physical activation owing to the lower temperatures and shorter time needed for activating material.ClassificationActivated carbons are complex products which are difficult to classify on the basis of their behaviour, surface characteristics and preparation methods. However, some broad classification is made for general purpose based on their physical characteristics.Powdered activated carbon (PAC)A micrograph of activated charcoal under bright field illumination on a light microscope. Notice the fractal-like shape of the particles hinting at their enormous surface area. Each particle in this image, despite being only around 0.1 mm wide, has a surface area of several square metres. This image of activated charcoal in water is at a scale of 6.236 pixels/μm, the entire image covers a region of approximately 1.1 by 0.7 mm.Traditionally, active carbons are made in particular form as powders or fine granules less than 1.0 mm in size with an average diameter between .15 and .25 mm.[2] Thus they present a large surface to volume ratio with a small diffusion distance. PAC is made up of crushed or ground carbon particles, 95–100% of which will pass through a designated mesh sieve or sieve. Granularactivated carbon is defined as the activated carbon being retained on a 50-mesh sieve (0.297 mm) and PAC material as finer material, while ASTM classifies particle sizes corresponding to an 80-mesh sieve (0.177 mm) and smaller as PAC. PAC is not commonly used in a dedicated vessel, owing to the high head loss that would occur. PAC is generally added directly to other process units, such as raw water intakes, rapid mix basins, clarifiers, and gravity filters.Granular activated carbon (GAC)Granular activated carbon has a relatively larger particle size compared to powdered activated carbon and consequently, presents a smaller external surface. Diffusion of the adsorbate is thus an important factor. These carbons are therefore preferred for all adsorption of gases and vapors as their rate of diffusion are faster. Granulated carbons are used for water treatment, deodorization and separation of components of flow system. GAC can be either in the granular form or extruded. GAC is designated by sizes such as 8×20, 20×40, or 8×30 for liquid phase applications and 4×6, 4×8 or 4×10 for vapor phase applications. A20×40 carbon is made of particles that will pass through a U.S. Standard Mesh Size No. 20 sieve (0.84 mm) (generally specified as 85% passing) but be retained on a U.S. Standard Mesh Size No. 40 sieve (0.42 mm) (generally specified as 95% retained). A WWA(1992) B604 uses the 50-mesh sieve (0.297 mm) as the minimum GAC size. The most popular aqueous phase carbons are the 12×40 and 8×30 sizes because they have a good balance of size, surface area, and head loss characteristics.Extruded activated carbon (EAC)Extruded activated carbon combines powdered activated carbon with a binder, which are fused together and extruded into a cylindrical shaped activated carbon block with diameters from 0.8 to 130 mm. These are mainly used for gas phase applications because of their low pressure drop, high mechanical strength and low dust content.Impregnated carbonPorous carbons containing several types of inorganic impregnant such as iodine, silver, cations such as Al, Mn, Zn, Fe, Li, Ca have also been prepared for specific application in air pollution control especially in museums and galleries. Due to antimicrobial/antiseptic properties, silver loaded activated carbon is used as an adsorbent for purification of domestic water. Drinking water can be obtained from natural water by treating the natural water with a mixture of activated carbon and Al(OH)3, a flocculating agent. Impregnated carbons are also used for the adsorption of H2S and thiols. Adsorption rates for H2S as high as 50% by weight have been reported.Polymer coated carbonThis is a process by which a porous carbon can be coated with a biocompatible polymer to give a smooth and permeable coat without blocking the pores. The resulting carbon is useful for hemoperfusion. Hemoperfusion is a treatment technique in which large volumes of the patient's blood are passed over an adsorbent substance in order to remove toxic substances from the blood.OtherActivated carbon is also available in special forms such as cloths and fibres. The "carbon cloth" for instance is used in personnel protection for the military.PropertiesA gram of activated carbon can have a surface area in excess of 500 m2, with 1500 m2being readily achievable.[3] Carbon aerogels, while more expensive, have even higher surface areas, and are used in special applications.Activated carbon, as viewed by an electron microscopeUnder an electron microscope, the high surface-area structures of activated carbon are revealed. Individual particles are intensely convoluted and display various kinds of porosity; there may be many areas where flat surfaces of graphite-like material run parallel to each other, separated by only a few nanometers or so. These micropores provide superb conditions for adsorption to occur, since adsorbing material can interact with many surfaces simultaneously. Tests of adsorption behaviour are usually done with nitrogen gas at 77 K under high vacuum, but in everyday terms activated carbon is perfectly capable of producing the equivalent, by adsorption from its environment, liquid water from steam at 100 °C and a pressure of 1/10,000 of an atmosphere.James Dewar, the scientist after whom the Dewar (vacuum flask) is named, spent much time studying activated carbon and published a paper regarding its absorption capacity with regard to gases.[4]In this paper, he discovered that cooling the carbon to liquid n itrogen temperatures allowed it to absorb significant quantities of numerous air gases, among others, that could then be recollected by simply allowing the carbon to warm again and that coconut based carbon was superior for the effect. He uses oxygen as an example, wherein the activated carbon would typically absorb the atmospheric concentration (21%) under standard conditions, but release over 80% oxygen if the carbon was first cooled to low temperatures.Physically, activated carbon binds materials by van der Waals force or London dispersion force.Activated carbon does not bind well to certain chemicals, including alcohols, glycols, strong acids and bases, metals and most inorganics, such as lithium, sodium, iron, lead, arsenic, fluorine, and boric acid.Activated carbon does adsorb iodine very well and in fact the iodine number, mg/g, (ASTM D28 Standard Method test) is used as an indication of total surface area.Contrary to a claim repeated[citation needed]throughout the web, activated carbon does not absorb ammonia.Carbon monoxide is not well absorbed by activated carbon. This should be of particular concern to those using the material in filters for respirators, fume hoods or other gas control systems as the gas is undetectable to the human senses, toxic to metabolism and neurotoxic.Substantial lists of the common industrial and agricultural gases absorbed by activated carbon can be found online.[5]Activated carbon can be used as a substrate for the application of various chemicals to improve the adsorptive capacity for some inorganic (and problematic organic) compounds such as hydrogen sulfide(H2S), ammonia (NH3), formaldehyde (HCOH), radioisotopes iodine-131(131I) and mercury (Hg). This property is known as chemisorption.Iodine numberMany carbons preferentially adsorb small molecules. Iodine number is the most fundamental parameter used to characterize activated carbon performance. It is a measure of activity level (higher number indicates higher degree of activation), often reported in mg/g (typical range 500–1200 mg/g). It is a measure of the micropore content of the activated carbon (0 to 20 Å, or up to 2 nm) by adsorption of iodine from solution. It is equivalent to surface area of carbon between 900 m²/g and 1100 m²/g. It is the standard measure for liquid phase applications.Iodine number is defined as the milligrams of iodine adsorbed by one gram of carbon when the iodine concentration in the residual filtrate is 0.02 normal. Basically, iodine number is a measure of the iodine adsorbed in the pores and, as such, is an indication of the pore volume available in the activated carbon of interest. Typically, water treatment carbons have iodine numbers ranging from 600 to 1100. Frequently, this parameter is used to determine the degree of exhaustion of a carbon in use. However, this practice should be viewed with caution as chemical interactions with the adsorbate may affect the iodine uptake giving false results. Thus, the use of iodine number as a measure of the degree of exhaustion of a carbon bed can only be recommended if it has been shown to be free of chemical interactions with adsorbates and if an experimental correlation between iodine number and the degree of exhaustion has been determined for the particular application.MolassesSome carbons are more adept at adsorbing large molecules. Molasses number or molasses efficiency is a measure of the mesopore content of the activated carbon (greater than 20 Å, or larger than 2 nm) by adsorption of molasses from solution. A high molasses number indicates a high adsorption of big molecules (range 95–600). Caramel dp (decolorizing performance) is similar to molasses number. Molasses efficiency is reported as a percentage (range 40%–185%) and parallels molasses number (600 = 185%, 425 = 85%). The European molasses number (range 525–110) is inversely related to the North American molasses number.Molasses Number is a measure of the degree of decolorization of a standard molasses solution that has been diluted and standardized against standardized activated carbon. Due to the size of color bodies, the molasses number represents the potential pore volume available for larger adsorbing species. As all of the pore volume may not be available for adsorption in a particular waste water application, and as some of the adsorbate may enter smaller pores, it is not a good measure of the worth of a particular activated carbon for a specific application. Frequently, this parameter is useful in evaluating a series of active carbons for their rates of adsorption. Given two active carbons with similar pore volumes for adsorption, the one having the higher molasses number will usually have larger feeder pores resulting in more efficient transfer of adsorbate into the adsorption space.T anninTannins are a mixture of large and medium size molecules. Carbons with a combination of macropores and mesopores adsorb tannins. The ability of a carbon to adsorb tannins is reported in parts per million concentration (range 200 ppm–362 ppm).Methylene blueSome carbons have a mesopore (20 Å to 50 Å, or 2 to 5 nm) structure which adsorbs medium size molecules, such as the dye methylene blue. Methylene blue adsorption is reported in g/100g(range 11–28 g/100g).DechlorinationSome carbons are evaluated based on the dechlorination half-value length, which measures the chlorine-removal efficiency of activated carbon. The dechlorination half-value length is the depth of carbon required to reduce the chlorine level of a flowing stream from 5 ppm to 3.5 ppm. A lower half-value length indicates superior performance.Apparent densityHigher density provides greater volume activity and normally indicates better quality activated carbon.Hardness/abrasion numberIt is a measure of the activated carbon’s resistance to attrition. It is important indicator of activated carbon to maintain its physical integrity and withstand frictional forces imposed by backwashing, etc. There are large differences in the hardness of activated carbons, depending on the raw material and activity level.Ash contentIt reduces the overall activity of activated carbon. It reduces the efficiency of reactivation. The metal oxides (Fe2O3) can leach out of activated carbon resulting in discoloration. Acid/water soluble ash content is more significant than total ash content. Soluble ash content can be very important for aquarists, as ferric oxide can promote algal growths. A carbon with a low soluble ash content should be used for marine, freshwater fish and reef tanks to avoid heavy metal poisoning and excess plant/algal growth.Carbon tetrachloride activityMeasurement of the porosity of an activated carbon by the adsorption of saturated carbon tetrachloride vapour.Particle size distributionThe finer the particle size of an activated carbon, the better the access to the surface area and the faster the rate of adsorption kinetics. In vapour phase systems this needs to be considered against pressure drop, which will affect energy cost. Careful consideration of particle size distribution can provide significant operating benefits.Examples of adsorptionHeterogeneous catalysisThe most commonly encountered form of chemisorption in industry, occurs when a solid catalyst interacts with a gaseous feedstock, the reactant/s. The adsorption of reactant/s to the catalyst surface creates a chemical bond, altering the electron density around the reactant molecule and allowing it to undergo reactions that would not normally be available to it.Adsorption refrigerationAdsorption refrigeration and heat pump cycles rely on the adsorption of a refrigerant gas into an adsorbent at low pressure and subsequent desorption by heating. The adsorbent acts as a "chemicalcompressor" driven by heat and is, from this point of view, the "pump" of the system. It consists of a solar collector, a condenser or heat-exchanger and an evaporator that is placed in a refrigerator box. The inside of the collector is lined with an adsorption bed packed with activated carbon adsorbed with methanol. The refrigerator box is insulated filled with water. The activated carbon can adsorb a large amount of methanol vapours in ambient temperature and desorb it at a higher temperature (around 100 degrees Celsius). During the daytime, the sunshine irradiates the collector, so the collector is heated up and the methanol is desorbed from the activated carbon. In desorption, the liquid methanol adsorbed in the charcoal heats up and vaporizes. The methanol vapour condenses and is stored in the evaporator.At night, the collector temperature decreases to the ambient temperature, and the charcoal adsorbs the methanol from the evaporator. The liquid methanol in the evaporator vaporizes and absorbs the heat from the water contained in the trays. Since adsorption is a process of releasing heat, the collector must be cooled efficiently at night. As mention ed above, the adsorption refrigeration system operates in an intermittent way to produce the refrigerating effect.Helium gas can also be 'pumped' by thermally cycling activated carbon 'sorption pumps' between 4 kelvins and higher temperatures. An example of this is to provide the cooling power for the Oxford Instruments AST series dilution refrigerators. 3He vapour is pumped from the surface of the dilute phase of a mixture of liquid 4He and its isotope 3He. The 3He is adsorbed onto the surfaces of the carbon at low temperature (typically <4K), the regeneration of the pump between 20 and 40 K returns the 3He to the concentrated phase of the liquid mixture. Cooling occurs at the interface between the two liquid phases as 3He 'evaporates' across the phase boundary. If more than one pump is present in the system a continuous flow of gas and hence constant cooling power can be obtained, by having one sorption pump regenerating while the other is pumping. Systems such as this allow temperatures as low as 10 mK (0.01 kelvin) to be obtained with very few moving parts.ApplicationsActivated carbon is used in gas purification, gold purification, metal extraction, water purification, medicine, sewage treatment, air filters in gas masks and respirators, filters in compressed air and many other applications.One major industrial application involves use of activated carbon in the metal finishing field. It is very widely employed for purification of electroplating solut ions. For example, it is a main purification technique for removing organic impurities from bright nickel plating solutions. A variety of organic chemicals are added to plating solutions for improving their deposit qualities and for enhancing properties like brightness, smoothness, ductility, etc. Due to passage of direct current and electrolytic reactions of anodic oxidation and cathodic reduction, organic additives generate unwanted break down products in solution. Their excessive build up can adversely affect the plating quality and physical properties of deposited metal. Activated carbon treatment removes such impurities and restores plating performance to the desired level.Analytical chemistry applicationsActivated carbon, in 50% w/w combination with celite, is used as stationary phase in low-pressure chromatographic separation of carbohydrates (mono-, di- trisacchardes) using ethanol solutions(5–50%) as mobile phase in analytical or preparative protocols.Environmental applicationsActivated carbon is usually used in water filtration systems. In this illustration, the activated carbon is in the fourth level (counted from bottom).Carbon adsorption has numerous applications in removing pollutants from air or water streams both in the field and in industrial processes such as:▪Spill cleanup▪Groundwaterremediation▪Drinking waterfiltration▪Air purification▪V olatile organic compounds capture from painting, dry cleaning, gasoline dispensing operations, and other processes.In 2007, West-Flanders University (in Belgium) began research in water treatment after festivals.[6] A full scale activated carbon installation was built at the Dranouter music festival in 2008, with plans to utilize the technology to treat water at this festival for the next 20 years.[6]Activated charcoal is also used for the measurement of radon concentration in air.Medical applicationsActivated carbon is used to treat poisonings and overdoses following oral ingestion.It is thought to bind to poison and prevent its absorption by the gastrointestinal tract. In cases of suspected poisoning, medical personnel administer activated charcoal on the scene or at a hospital's emergency department. Dosing is usually empirical at 1 gram/kg of body mass (for adolescents or adults, give 50–100 g), usually given only once, but depending on the drug taken, it may be given more than once. In rare situations activated charcoal is used in Intensive Care to filter out harmful drugs from the blood stream of poisoned patients. Activated charcoal has become the treatment of choice for many poisonings, and other decontamination methods such as ipecac-induced emesis or stomach pumping are now used rarely.Activated charcoal for medical use.While activated carbon is useful in acute poisoning, it has been shown to not be effective in long term accumulation of toxins, such as with the use of toxic herbicides.[7]Mechanisms of action:▪Binding of the toxin to prevent stomach and intestinal absorption. Binding is reversible soa cathartic such as sorbitol may be added as well.▪It interrupts the enterohepatic and enteroenteric circulation of some drugs/toxins and their metabolitesIncorrect application (e.g. into the lungs) results in pulmonary aspiration which can sometimes be fatal if immediate medical treatment is not init iated.[8]The use of activated charcoal is contraindicated when the ingested substance is an acid, an alkali, or a petroleum product.For pre-hospital (paramedic) use, it comes in plastic tubes or bottles, commonly 12.5 or 25 grams, pre-mixed with water. The trade names include InstaChar, SuperChar, Actidose, Charcodote, and Liqui-Char, but it is commonly called activated charcoal.Ingestion of activated charcoal prior to consumption of alcoholic beverages appeared to reduce absorption of ethanol into the blood. 5 to 15 milligrams of charcoal per kilogram of body weight taken at the same time as 170 ml of pure ethanol (which equals to about 10 servings of an alcoholic beverage), over the course of one hour, seemed to reduce potential blood alcohol content.[9] Y et other studies showed that this is not the case, and that ethanol blood concentrations were increased because of activated charcoal use.[10]Charcoal biscuits were sold in England starting in the early 19th century, originally as an antidote to flatulence and stomach trouble.[11]Tablets or capsules of activated charcoal are used in many countries as an over-the-counter drug to treat diarrhea, indigestion, and flatulence.[12]There is some evidence of its effectiveness as a treatment for irritable bowel syndrome (IBS),[13]and to prevent diarrhea in cancer patients who have received irinotecan.[14] It can interfere with the absorbency of some medications, and lead to unreliable readings in medical tests such as the guaiac card test.[15] Activated charcoal is also used for bowel preparation by reducing intestinal gas content before abdominal radiography to visualize bile and pancreatic and renal stones. A type of charcoal biscuit has also been marketed as a pet care product.Fuel storageResearch is being done testing various activated carbons' ability to store natural gas and hydrogen gas. The porous material acts like a sponge for different types of gasses. The gas is attracted to the carbon material via V an der Waals forces. Some carbons have been able to achieve bonding energies of 5–10 kJ per mol. The gas may then be desorbed when subjected to higher temperatures and either combusted to do work or in the case of hydrogen gas extracted for use in a hydrogen fuel cell. Gas storage in activated carbons is an appealing gas storage method because the gas can be stored in a low pressure, low mass, low volume environment that would be much more feasible than bulky on board compression tanks in vehicles. The United States Department of Energy has specified certain goals to be achieved in the area of research and development of nano-porous carbon materials. As of yet all of the goals are yet to be satisfied but numerous institutions, including the Alliance for Collaborative Research in Alternative Fuel Technology (ALL-CRAFT, ) program, are continuing to conduct work in this promising field.Gas purificationFilters with activated carbon are usually used in compressed air and gas purification to remove oil vapors, odors, and other hydrocarbons from the air. The most common designs use a 1 stage or 2 stage filtration principle in which activated carbon is embedded inside the filter media. Activated charcoal is also used in spacesuit Primary Life Support Systems. Activated charcoal filters are used to retain radioactive gases from a nuclear boiling water reactor turbine condenser. The air vacuumed from the condenser contains traces of radioactive gases. The large charcoal beds adsorb these gases and retains them while they rapidly decay to non-radioactive solid species. The solids are trapped in the charcoal particles, while the filtered air passes through.Chemical purificationActivated carbon is commonly used to purify homemade non-dangerous chemicals such as sodium acetate.Distilled alcoholic beverage purificationSee also: Lincoln County ProcessActivated carbon filters can be used to filter vodka and whiskey of organic impurities which can affect color, taste, and odor. Passing an organically impure vodka through an activated carbon filter at the proper flow rate will result in vodka with an identical alcohol content and significantly increased organic purity, as judged by odor and taste.[citation needed]Mercury scrubbingActivated carbon, often impregnated with iodine or sulfur, is widely used to trap mercury emissions from coal-fired power stations, medical incinerators, and from natural gas at the wellhead. This carbon is a specialty product costing more than US$4.00 per kg. However, it is often not recycled.Disposal in the USA after absorbing mercuryThe mercury laden activated carbon presents a disposal dilemma.[citation needed]If the activated carbon contains less than 260 ppm mercury, Federal regulations allow it to be stabilized (for example, trapped in concrete) for landfilling.[citation needed] However, waste containing greater than 260 ppm is considered to be in the high mercury subcategory and is banned from landfilling (Land-Ban Rule).[citation needed] It is this material which is now accumulating in warehouses and in deep abandoned mines at an estimated rate of 1000 tons per year.[citation needed]The problem of disposal of mercury laden activated carbon is not unique to the U.S. In the Netherlands this mercury is largely recovered[16] and the activated carbon is disposed by complete burning.RegenerationThe regeneration of activated carbons involves restoring the adsorptive capacity of saturated activated carbon by desorbing adsorbed contaminants on the activated carbon surface.Thermal regenerationThe most common regeneration technique employed in industrial processes is thermal regeneration.[17] The thermal regeneration process generally follows three steps [18]:▪Adsorbent drying at approximately 105 °C▪High temperature desorption and decomposition (500–900°C) under an inert atmosphere ▪Residual organic gasification by an oxidising gas (steam or carbon dioxide) at elevated temperatures (800°C)The heat treatment stage utilises the exothermic nature of adsorption and results in desorption, partial cracking and polymerization of the adsorbed organics. The final step aims to remove charred organic residue formed in the porous structure in the previous stage and re-expose the。

多孔介质内油水流动阻力系数实验分析

多孔介质内油水流动阻力系数实验分析

多孔介质内油水流动阻力系数实验分析吴国忠;邢永强;吕妍;齐晗兵;李栋【摘要】Based on resistance coefficient measuring device of oil and water migration in porous medium,taking water and oil as working fluid, the resistance characteristics of water and oil flow in homogeneous approximation and mixed grain particle size glass ball channel were measured,and the velocity and pressure drop curve expression was calculated,and then viscous and inertia resistance coefficients of water and oil flow in glass ball were established. The results show that the inertia resistance of single phase medium is significantly smaller than that by mixing particle size,and the effect of viscous drag is larger than that by mixing particle size.The inertia and viscous drag of multiphase medium through uniform particle size porous media region are less than those with the mixed size.Under the same particle diameter,the inertial resistance effect of multiphase medium is obviously more than that of single-phase medium,but its viscous resistance is weak compared with single-phase medium.%基于多孔介质油水迁移的阻力系数测量装置,以水和油为工质,测量了其在近似均匀、混合粒径玻璃球通道内的流动阻力特性,并拟合了速度-压降的曲线关系表达式,计算得到了黏性、惯性阻力系数。

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On the Physical ProperƟes of Apparent Two-Phase Fractal Porous Media
Boming Yu,* Jianchao Cai, and Mingqing Zou
:F
In this study, we summarized some basic characters of fractal porous media, including the fractal pore or par cle size distribu on, pore or par cle density func on, the fractal dimensions for the pore and solid phases, and their rela ons. The geometric porosi es vs. the fractal dimensions and microstructures of porous media were reviewed and discussed in two and three dimensions. The specific surface areas of fractal porous media in two and three dimensions were derived and were expressed as a func on of the fractal dimensions and microstructural parameters. The fluid velocies in fractal porous media were also derived and found to be a func on of the fractal dimensions and microstructural parameters of the medium. The parameters presented are the fundamental ones and may have poten al in analysis of transport proper es in fractal porous media.
All rights reserved. No part of this periodical may be reproduced or transmi ed in any form or by any means, electronic or mechanical, including photocopying, recording, or any informa on storage and retrieval system, without permission in wri ng from the publisher.
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· Vol. 8, No. 1, February 2009
review of the fractal models of fragmented and aggregated soils based on the Sierpinski carpet geometry and applied two different models to represent a fractal porous medium, as shown in Fig. 1, which shows third-iteration Sierpinski carpets. In Fig. 1a, the black represents the solid phase, which is fractal, while the white gaps represent pores, which are not fractal. In Fig. 1b, the white represents the pore phase, which is fractal, while the black spots represent solids, which are not fractal. Perrier et al. (1999) presented an independent and similar study. It is worth pointing out that the Sierpinski carpet, as shown in Fig. 1, is a single-phase fractal medium. Figure 1 will be discussed further below. Compared with single-phase (or saturated) transport phenomena in porous media, multiphase (or two-phase) immiscible flows (or transport) in porous media are not well understood yet. Multiphase immiscible flows in porous media are very important in practical applications such as the petroleum industry, chemical engineering, and soil engineering. The single (saturated) porous medium is, in fact, only a special case of a two-phase (unsaturated) porous medium. The fractal dimensions for two-phase (unsaturated) porous media might be more fundamental than some macroscopic parameters such as permeability and porosity. The reviews by Rieu and Perrier (1998) and Perrier et al. (1999), however, did not involve a two-phase fractal medium. This work summarizes some fundamentals about singlephase and two-phase fractal porous media in a more general way. The relationships among the fractal dimensions, porosities, specific surface areas, and fractal velocity with the microstructure of porous media are derived and discussed below.
particles, and geometric structures. Some researchers (Bear, 1972; Kaviany, 1995) have modified the Kozeny–Carman equation as a function of porosity φ, specific surface area S, and tortuosity τ (defined as the ratio of the real length to the straight-line length). The Kozeny–Carman equation has been hotly debated since its inception due to its dependence on the microstructures of porous media. Another example is the thermal conductivity of porous media; available results (Hsu et al., 1995; Feng et al., 2004) show that the thermal conductivity of a porous medium is related not only to the porosity but also to the microstructures of the porous medium. The dielectric constant of porous ultra-low-k (dielectric constant) dielectrics has also been found to be a function of porosity and pore size distributions (Nakano et al., 1993; Beckers and de Leeuw, 2001). Since its establishment by Mandelbrot (1982), fractal geometry has attracted considerable interest in many disciplines for its ability to characterize irregular and disordered objects such as, for example, porous media (Katz and Thompson, 1985; Gimenez et al., 1997; Yu and Li, 2001; Yu and Cheng, 2002; Perfect, 2005) and the roughness of surfaces (Majumdar, 1992), rocks, and fractures (Sahimi, 1993, 1995; Adler and Thovert, 1998; Berkowitz, 2002). Katz and Thompson (1985) might have been the first to present experimental evidence indicating that the pore spaces of a set of sandstone samples are fractals and are self-similar across three to four orders of magnitude in length extending from 1 nm to 100 μm. They argued that the pore volume is a fractal with the same fractal dimension as the pore–rock interface. They also obtained an empirical correlation for the fractal dimension of pore spaces. Rieu and Perrier (1998) made a comprehensive
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