Effect of gas mixing ratio on etch behavior
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王鑫,毕海鑫,修伟业,等. 发酵蓝靛果果汁的工艺优化及香气成分分析[J]. 食品工业科技,2023,44(13):176−185. doi:10.13386/j.issn1002-0306.2022080121WANG Xin, BI Haixin, XIU Weiye, et al. Process Optimization and Aroma Composition Analysis of Fermented Lonicera edulis Juice[J]. Science and Technology of Food Industry, 2023, 44(13): 176−185. (in Chinese with English abstract). doi:10.13386/j.issn1002-0306.2022080121· 工艺技术 ·发酵蓝靛果果汁的工艺优化及香气成分分析王 鑫1,2,毕海鑫3,修伟业1,遇世友1,韩春然1,*(1.黑龙江省谷物食品与谷物资源综合加工重点实验室,哈尔滨商业大学食品工程学院,黑龙江哈尔滨 150028;2.黑龙江省林业科学院,黑龙江哈尔滨 150081;3.黑龙江东方学院食品工程学院,黑龙江哈尔滨 150060)摘 要:为解决蓝靛果口感酸涩、季节性强、储藏困难的问题,以酵母菌发酵生产发酵蓝靛果果汁,通过单因素及正交试验优化其发酵条件,并采用气相色谱-质谱联用技术(GC-MS ),研究最优条件下发酵过程中,发酵蓝靛果果汁香气成分的变化。
结果显示,蓝靛果果汁的最优发酵条件为:发酵温度18 ℃、发酵时间8 d 、酵母菌添加量1.0%。
此条件下,感官评分为93.10±2.73分;利用该最优条件发酵蓝靛果果汁,在发酵过程中共检测到香气物质62种,采用主成分分析法分析共得到4个主成分,其中前3个主成分的累计方差贡献率为88.64%,癸酸乙酯、乙酸乙酯、9-癸烯酸乙酯、己酸乙酯、庚酸和异戊醇为发酵过程中果汁的主要香气成分。
油气采收率技术1998年9月8用驱油效率实验优选矿场应用的聚合物分子量及用量谢 峰 皇海权(河南石油勘探局勘探开发研究院)摘要 用不同分子量、不同浓度的聚丙烯酰胺(H PAM)溶液在人造岩心上进行较系统的驱油实验,结果表明:(1)分子量越高,或浓度越大,溶液的增粘性就越强,驱油效率也越高;(2)当分子量和溶液粘度相同时,驱油效率随残余阻力系数的增加而提高;(3)当注入溶液的孔隙体积一样时,每吨聚合物的增油量随溶液浓度的增加而下降。
以岩心做的驱油效率实验为基础,用简便方法优选出适合河南油田的聚合物分子量为1430万,用量为320PV・m g L。
在河南油田面积为3101km2的聚合物驱矿场先导试验中,经三年零二个月的试验,全区增油4185×104t,提高采收率9119%,每吨聚合物增油210t,取得了很好的经济效益。
主题词 聚合物 驱油效率 优选 分子量 用量 溶液 粘度 采收率自由词 残余阻力系数0 引 言聚合物驱油是一种技术上成熟的三次采油方法,在我国许多油田得到推广应用。
河南油田在开展聚合物驱工作中,首先针对油层条件筛选合适的聚合物产品,尔后对其性能进行系统的评价,确定用量。
聚合物驱油效率的研究是整个评价工作的核心。
聚合物驱油时,溶液浓度、分子量、粘度和滞留在岩石孔道中的聚合物分子都是影响其驱油能力的重要因素,弄清它们与驱油效率的内在关系,对优选合适的聚合物分子量和确定其合理用量,确保在矿场应用中取得较高的经济效益是十分重要的。
1 实验部分111 实验条件(1)实验用的岩心是 25c m×8c m规格的石英砂人造岩心;(2)岩心参数:孔隙度为21%~31%,渗透率为110~114Λm2;(3)原油粘度为718m Pa・s,水粘度为0142m Pa・s;(4)聚合物溶液:用日本三井氰胺公司提供的不同分子量的粉状聚丙烯酰胺配制而成。
112 实验内容把制备的岩心抽空,饱和水,用原油驱水造成束缚水,水驱至含水率为98%,改注一定体收稿日期:1997210228积和不同分子量的聚合物溶液,然后再水驱直到出口无原油流出为止。
The effect of pressure on gassolubility气压对气体溶解度的影响在日常生活中,我们经常会感受到气压的变化,比如搭乘高速列车时耳朵发痛,登高时呼吸困难等等。
除了这些显而易见的感觉外,气压变化对其他方面的影响也是不容忽视的。
本文将重点探讨气压对气体溶解度的影响。
一、气体溶解度的定义和计算在化学中,溶解度指的是一种物质在一定条件下溶解于另一种物质中的最大量。
气体的溶解度则指的是气体在液体或固体中的溶解度。
具体计算方法可参考亨利定律,该定律指出在一定温度下,气体在液体中的溶解度与气体分压成正比。
单位时间内气体分子从气相转移到溶液中的速度称为气体的溶解速率,公式为:R=kP其中,R为溶解速率,k为比例系数,P为气体分压。
为了比较不同气体在同一条件下的溶解度,通常使用气体的摩尔溶解度进行计算。
它的定义为单位质量溶剂中溶质分子数的摩尔数。
显然,摩尔溶解度与分压和溶解速率之间的关系是密不可分的。
二、气压对气体溶解度的影响气压是指单位面积上垂直于该面积方向的力的大小。
在常温下,气体的分子运动速度远远高于液体或固体的分子运动速度。
因此,气体的分子往往呈自由分子状态,在空气压力的作用下,随机撞击容器内壁,产生压强。
而当容器顶部为液体或固体时,气体分子产生的撞击会使溶解在液体或固体中的气体分子发生溶解和析出的动态平衡。
这就是溶解的基本过程。
气体溶解度受气压的影响非常明显。
由于液体是固体和气体之间的中介体,并且气体分子在空气压力下会产生压强,因此气压的变化会导致气体的分压发生变化,对气体溶解度产生直接影响。
亨利定律表明溶解度与气体的分压成正比,因此气压越高,气体的分压就越高,气体分子进入液体或固体中的速度也就越快,气体的溶解度就越大。
反之,气压越小,气体的分压就越小,气体分子进入液体或固体中的速度也就越慢,气体的溶解度也就越小。
三、应用了解气体溶解度的影响因素及其计算方法,对于一些实际问题的解决具有重要意义。
低浓度含氧煤层气吸附富集过程中吸附塔高径比的影响规律李永玲;刘应书【摘要】根据Coward爆炸三角形提出一种安全的分离富集低浓度含氧煤层气的设想——等比例变压吸附法,通过实验证明采用活性炭和碳分子筛作为混合吸附剂,可以在保证解吸气、排放气中甲烷浓度和氧气浓度不进入爆炸范围的前提下将煤层气中的甲烷浓度从20%富集到30%以上.实验研究了吸附塔高径比对解吸气和排放气中甲烷、氧气的浓度分布以及高径比对反吹时间的影响.结果表明提高高径比、增加反吹过程均能降低排放气和解吸气的爆炸性,实现低浓度含氧煤层气安全富集的可行性.但高径比过大,吸附时间过长,单位时间内吸附循环数减少,会降低吸附剂的利用率,增大床层阻力,增加压缩机能耗.【期刊名称】《煤炭学报》【年(卷),期】2014(039)003【总页数】6页(P492-497)【关键词】低浓度;含氧煤层气;高径比;变压吸附【作者】李永玲;刘应书【作者单位】北京科技大学机械工程学院,北京100083;北京科技大学机械工程学院,北京100083【正文语种】中文【中图分类】TD712;TD989目前,我国每年因采煤向空气中排放大量的煤层气,同时由于我国煤层气有着“三高一低”的特点,很难像美国、澳大利亚那样大规模的采用地面开发的方式,而主要采用井下抽放的方式进行,致使我国煤矿抽放的煤层气浓度普遍较低。
2008年煤层气抽采量约58亿m3,而井下抽放量近53亿m3,但井下抽放的甲烷浓度(全文均指体积分数)在20%~65%[1-3]。
对于低浓度煤层气(甲烷浓度<30%),出于安全考虑,通常被禁止直接利用[4],致使煤矿区抽采的煤层气利用率非常低[5],目前国内低浓度煤层气主要采用焚烧销毁或者放散的办法处理。
然而甲烷的温室效应是CO2的21倍,对臭氧层的破坏能力是CO2的7倍,甲烷对全球气候变暖的贡献占15%,仅次于CO2[6]。
因此这种处理方式不仅浪费了大量的优质能源,而且造成了温室气体的排放,对大气环境造成极大的破坏。
乙烯裂解炉耦合模拟中湍流模型的影响分析倪城振;杜文莉;胡贵华【摘要】配备底部烧嘴和侧壁烧嘴的乙烯裂解炉应用越来越广泛,不同燃烧模式影响着炉膛内湍流流动状态,考虑到裂解炉中湍流流动与燃气喷料、燃烧和传热有较强的非线性耦合作用,为此探究不同湍流模型在裂解炉/反应器耦合模拟中的影响对于裂解炉的精确设计和优化至关重要.针对不同湍流模型对某十万吨工业乙烯裂解炉进行了耦合模拟,利用CFD数值模拟对采用标准k-ε模型、RNG k-ε和Realizable k-ε模型所建立的湍流流动模型进行评估.将三种湍流模型的模拟结果与工业数据进行比较,重点分析了裂解炉内的速度、温度、湍流能力等参数的分布情况,表明Realizable k-ε模型在火焰稳定性、反应效率等方面优于其他两种模型,且基于Realizable k-ε湍流方程的反应管模型在热通量、炉管外壁温度分布计算结果更接近实际工况.【期刊名称】《化工学报》【年(卷),期】2019(070)002【总页数】11页(P450-459,封2)【关键词】湍流;计算流体力学;数值模拟;乙烯裂解炉;反应器耦合【作者】倪城振;杜文莉;胡贵华【作者单位】华东理工大学信息科学与工程学院,上海200237;华东理工大学信息科学与工程学院,上海200237;华东理工大学化工过程先进控制和优化技术教育部重点实验室,上海200237;华东理工大学化工过程先进控制和优化技术教育部重点实验室,上海200237【正文语种】中文【中图分类】TQ021.1;TE963引言目前,配备底部烧嘴和侧壁烧嘴的裂解炉在乙烯生产的化工装置得到越来越多的应用[1]。
一般工业情况下,裂解炉中底部烧嘴的燃烧是未预先混合的,而侧壁烧嘴的燃烧是预先混合的,这对炉膛内湍流流动状态存在很大影响。
乙烯裂解炉与反应器内的过程都呈强耦合关系[1-2],裂解炉辐射段发生的反应过程将影响其模型性能。
乙烯裂解炉内流动属于高Reynolds数湍流流动,其中发生的物理化学反应非常复杂,包括了燃烧、传热与组分输运等过程,湍流流动与燃气喷料、燃烧和传热有较强的非线性耦合作用。
导流筒高度对气固环流反应器流动特性的影响牛犁;刘梦溪;孟振亮【摘要】To study the effect of the height of the draft tube on the loop reactor flow characteristics, the model of a gas-solidcirculating fluidized bed in a loop reactor was established based on Euler - Euler method using Energy Minimization Multiscale(EMMS) drag force model with the particle kinetic theory. The appropriate model parameters were determined by comparing the experimental data.The height of draft tubes was studied and optimized using the established model and the effects of changes of the height of the draft tubeon the average bed density, mass flow rate and other factors were investigated. Results showed that the gas-solid airlift loop reactor(GSALR) with a 1.4 m high draft tube performed better and an average mass flow rate was higher than that of the original device with a 1.2 m draft tube by 36.17%.%为了研究导流筒高度对环流反应器内流动特性的影响,基于欧拉-欧拉方法,采用基于多尺度结构的EMMS曳力模型,结合颗粒动力学理论,建立了环流反应器内气固两相流动模型,通过对比实验数据,确定了合适的模型参数.采用已建立的流动模型,对导流筒高度进行了优化研究,考察了导流筒高度变化对平均床层密度、质量流率和环流速率等参数的影响.结果表明,导流筒优化高度为1.4 m时,环流效果较好,其平均质量流率比原装置(HD为1.2 m)提高了36.17%.【期刊名称】《化学反应工程与工艺》【年(卷),期】2016(032)002【总页数】8页(P106-113)【关键词】气固环流反应器;数值模拟;结构优化;导流筒高度【作者】牛犁;刘梦溪;孟振亮【作者单位】中国石油大学(北京)重质油国家重点实验室,北京 102249;中国石油大学(北京)重质油国家重点实验室,北京 102249;中国石油大学(北京)重质油国家重点实验室,北京 102249【正文语种】中文【中图分类】TQ018;TQ052.5环流反应器(GSALR)是一种高效的多相反应设备,因其具有结构相对简单、相间接触与混合性能好、传质系数高和易于操作等优点,环流反应器在化学工业、生物工程、冶金化工及环保等相关领域已经得到了广泛应用[1]。
Effect of gas mixing ratio on etch behavior of ZrO2thinfilms in Cl2-based inductively coupled plasmasAlexander EfremovDepartment of Electronic Devices and Materials Technology,State University of Chemistry and Technology,7F.Engels St.,153000Ivanovo,RussiaNam-Ki MinDepartment of Control and Instrumentation Engineering,Korea University,Jochiwon,Chungnam339-700,South KoreaSun Jin YunElectronics and Telecommunications Research Institute,161Gajung-dong,Yusong-gu,Daejeon305-350,KoreaKwang-Ho Kwon a͒Department of Control and Instrumentation Engineering,Korea University,Jochiwon,Chungnam339-700,South Korea͑Received14July2008;accepted15September2008;published30October2008͒The analysis of the ZrO2thinfilm etch mechanism in the Cl2/Ar,Cl2/He,and Cl2/N2inductivelycoupled plasmas was carried out.It was found that an increase in additive gas fraction atfixed gaspressure and input power results in increasing ZrO2etch rate,which changes from1.2nm/min forpure Cl2plasma up to3.15,2.40,and2.31nm/min for80%Ar,N2,and He,ngmuirprobe diagnostics and zero-dimensional plasma modeling indicated that both plasma parameters andactive species kinetics are noticeably influenced by the initial composition of the gas mixture.Fromthe model-based analysis of etch kinetics,it was shown that,similarly to the case of BCl3-basedplasmas,the behavior of the ZrO2etch rate corresponds to the ion-flux-limited etch regime.©2008American Vacuum Society.͓DOI:10.1116/1.2998806͔I.INTRODUCTIONRecently,a range of high dielectric constant͑high-k͒ma-terials,namely,ZrO2,Ta2O5,HfO2,and TiO2,were inten-sively investigated as the gate dielectrics to substitute forSiO2in the complementary metal-oxide-semiconductortechnology.1–3Among these materials,the ZrO2combinessuch favorable properties as a high dielectric constant͑20–25͒,a wide band gap͑5–7eV͒,and a close thermal expan-sion coefficient with Si that results in good thermal stabilityof ZrO2/Si interfaces.Accordingly,the development of an anisotropic dry etch process for ZrO2thinfilms is an impor-tant task to be solved for obtaining an accurate pattern trans-fer as well as stable device parameters.The most of existing works reported on the ZrO2“dry”etching process were focused on the BCl3-based gas chem-istries.Particularly,Pelhos et al.4investigated the etch be-havior of Zr1−x Al x O y thinfilm in Cl2/BCl3plasma.Chang and co-workers5–7reported on the etch process of ZrO2thin film in both Cl2and Cl2/BCl3plasmas and provided the experimental data on the dependences of the etch rate on main operating conditions.Finally,in our previous works, the ZrO2etch process was analyzed by both experiments and modeling using BCl3/Ar,8BCl3/CHF3/Ar,9and BCl3/He ͑Ref.10͒chemistries.The results reported in Refs.4–10can be summarized as follows:͑1͒In both Cl2-and BCl3-based plasmas,the ZrO2etch rate is limited by the low volatility of Zr chlorides͑the melting points are772°C for ZrCl2and 437°C for ZrCl4͒.11The addition of BCl3to Cl2increases the ZrO2etch rate due to the extraction of oxygen from the oxide through the spontaneous reaction2BCl x+ZrO2→Zr +2BOCl x͑Refs.6and7͒.͑2͒The etch thresholds determined from the dependence of etch rate from the square root of ion energy in Cl2and BCl3plasmas are very close.5,7This prob-ably means that the BCl x radicals do work as a catalyst but not as the main chemically active species.͑3͒The main en-chants are the Cl atoms while the behavior of the ZrO2etch rate corresponds to the ion-flux-limited etch regime of ion-assisted chemical reaction.8–10The mixtures of Cl2with Ar,He,or N2are the frequently used as plasma-forming gases for dry patterning some metals and metal oxides.12An important feature of such systems is that the etch result can be optimized not only by varying the operating conditions,but also by adjusting the gas mixing ratio,which directly influences the balance between chemi-cal and physical etch pathways.Also,there are some works that reported an increase in the etch rates of Au,13MgO,14 Pt,15and many other materials with increasing fraction of additive gases.The objective of this study was to investigate the effects of Ar,He,or N2on the ZrO2etch behavior in the Cl2-based plasmas as well as to understand how the additive gas influences the ZrO2etch rate through the changes of plasma parameters,plasma compositions,and surface kinet-ics.a͒Electronic mail:kwonkh@korea.ac.kr14801480 J.Vac.Sci.Technol.A26…6…,Nov/Dec20080734-2101/2008/26…6…/1480/7/$23.00©2008American Vacuum SocietyII.EXPERIMENTAL AND MODELING DETAILSA.Experimental setupThe130-nm-thick ZrO2films were deposited on Si͑100͒substrates at150°C using a plasma-enhanced atomic layer deposition method.A detailed description on the deposition method and operating conditions is given in Ref.16.The experiments were performed in a planar inductively coupled plasma͑ICP͒reactor.8–10The reactor consisted of a cylindrical quartz chamber with a radius͑r͒of16cm and a five-turn copper coil located on a10-mm-thick horizontal quartz window.The coil was connected to a13.56MHz power supply via the matching network.The distance be-tween the quartz window and the bottom electrode͑l͒was 12.8cm.The bottom electrode was made from the anodized aluminum and was also connected to a13.56MHz power supply in order to control the dc bias voltage on the sub-strate.During the etching process,the temperature of the bottom electrode was stabilized at17°C by the circulation of de-ionized water.The experiments were performed under such operating parameters as total gas pressure͑p͒of 6mTorr,input ICP power͑W͒of600W,bias power͑W dc͒of50W,and total gasflow rate͑q͒of70SCCM͑SCCMdenotes cubic centimeter per minute at STP͒.The Cl2/Ar, Cl2/He,and Cl2/N2mixing ratios were set in the range of 0%–80%Ar,He,or N2by adjusting the partial gasflow rate of the components.The ZrO2samples were placed in the center of the bottom electrode and had the size of about2ϫ2cm2,which is much smaller than the area of the bottom electrode.In fact,this allows neglecting both loading effect and disturbance of plasma parameters by the etch products.In order to deter-mine the etch rates,the etched depths were measured using a surface profiler͑Alpha-step500,Tencor͒.For this purpose, we developed the line striping of the photoresist͑PR͒͑AZ1512,positive͒with the linewidth/spacing ratio of 2m/2m.The initial thickness of the PR layer was about 1.5m.Plasma diagnostics was performed by Langmuir probe ͑LP͒measurements and quadrupole mass spectrometry ͑QMS͒.The LP diagnostics was realized with a double probe ͑DLP2000,Plasmart Inc.͒.The probe was installed through the chamber wall-side view port,placed at4cm above the bottom electrode and centered in the radial direction.For the treatment of I-V curves in order to obtain electron tempera-ture͑T e͒and total positive ion density͑n+͒,we used the software supplied by the equipment manufacturer.The cal-culations were based on the double probe theory developed by Johnson and Malter,17and the Allen–Boyd–Reynolds ap-proximation for the ion saturation current density was used.18 The QMS measurements͑HPR-30,Hiden Analytical͒were realized in RGA mode delivering the data on neutral species only.B.Plasma modelingTo obtain the data on the steady-state densities of plasma active species,we used a simplified zero-dimensional model with a Maxwellian electron energy distribution function ͑EEDF͒͑Refs.19and20͒and with the experimental data on T e and n+as input parameters.Though in the nonequilibrium systems the real EEDFs are not exactly Maxwellian,the ap-plicability of such a simplification for the modeling of the Cl2-based low-pressure͑pϽ50mTorr͒inductive discharges was shown in many published works.For example,Refs.21 and22demonstrate an acceptable agreement between mea-sured and model-predicted plasma parameters for both Cl2 and Cl2/Ar plasmas obtained with the Maxwellian approxi-mation for EEDF in the close range of experimental condi-tions as used in this study.The modeling algorithm was based on the simultaneous solution of following equations.͑1͒The kinetic equations for both neutral ground-state and charged species in a steady-state͑dn/dt=0͒approxima-tion R F=͑B+G+1/R͒n,where R F is the average forma-tion rate for the given type of species,n is their volume-average density,B is the loss frequency in bulk plasma,G is the frequency of the heterogeneous loss,andR is the residence time.The set of reactions taken into account by the model is given in Table I.The rate coefficients for electron impact reactions͑R1–R13͒were calculated as k=ͩ2e m eͪ1/2͵thϱf M͑͒͑͒ͱd,͑1͒where f M͑͒is the Maxwellian EEDF,th is the threshold energy,and͑͒is the process cross section.23For the N2 molecules,we neglected the dissociation.24For the Cl at-oms,we assumedBӶG=͓͑⌳2/D͒+͑2r/0.25␥ClT͔͒−1,25 where␥ClϷ0.05͑Ref.26͒is the recombination probabil-ity,⌳−2=͑2.405/r͒2+͑/l͒2is the effective diffusion length,19andT=͑8k B T/m Cl͒1/2.The effective diffusion coefficient was calculated as D−1=D f−1+D in−1,where D f is the free diffusion coefficient,and D in is the interdiffusion coefficient given by the Chapman–Enskog equation to-T ABLE I.Simplified reaction set for the modeling of Cl2/Ar,Cl2/He,and Cl2/N2plasmas.No.SchemeRate coefficient,thresholdenergyR1Cl2+e→Cl2++2e11.5eVR2Cl2+e→Cl−+Cl++e12.0eVR3Cl2+e→Cl+Cl++2e12.6eVR4Cl2+e→Cl2−→Cl+Cl−¯R5Cl2+e→Cl2*͑B3⌸͒→Cl+Cl+e 3.0eVR6Cl+e→Cl++2e13.5eVR7Cl−+e→Cl+2e 3.4eVR8Ar+e→Ar++2e15.8eVR9Ar+e→Ar m͑3P0,3P1,3P2͒+e11.55eVR10He+e→He++2e24.6eVR11He+e→He m͑1S0,3S1͒+e19.8eVR12N2+e→N2++2e15.6eVR13N2+e→N2͑A3⌺u+͒+e 6.17eVR14Cl−+n+͑Cl2+,Cl+,Ar+,He+,N2+→n+Cl͒ 5.0ϫ10−8cm3/sR15n+͑Cl2+,Cl+,Ar+,He+,N2+͒→wall/d cR16Cl͑g͒+Cl͑s͒→Cl2͑s͒→Cl2͑g͒r Clϳ0.05JVST A-Vacuum,Surfaces,and Filmsgether with Blanc’s law.21,22For simplicity,we assumed the temperature of the neutral particles ͑T ͒to be indepen-dent of gas mixing ratio and to be equal to 700K.19,21For negative ions,we applied G =0.19For positive ions,we used G Ϸ/d c with d c =0.5rl /͑rh l +lh r ͒.22The ion Bohmvelocitieswere calculated as =ͱeT e ͑1+s ͒/m i ͑1+s ␥T ͒,where s =͓exp ͑͑1+s ͒͑␥T −1͒/2͑1+s ␥T ͔͒͒−1͑Refs.19and 27͒is the relative den-sity of negative ions at the plasma sheath edge,␥T =T e /T i ,and =n Cl −/n e is the bulk electronegativity.Simi-larly with Refs.20and 21,we assumed equal tempera-tures for all kinds of ions T i ϷT +͑0.5−T ͒/p ,where T is the gas temperature in eV and p is in mTorr.The correc-tion factors h l and h r for the radial and axial sheath sizes are given by the low-pressure ഛ͑T i /T e ͒͑R ,L ͒diffusion theory.27͑2͒The quasineutrality conditions for volume densities of charged species ͑n e +n Cl −=n +,where n +=n Cl 2++n Cl ++n X +and n X +=n Ar +,n He +,or n N 2+͒,as well as for their fluxes tothe reactor walls ͑⌫e =⌫Cl 2++⌫Cl ++⌫X +,where ⌫X +=⌫Ar +,⌫He +,or ⌫N 2+͒.III.RESULTS AND DISCUSSIONFrom several published works,28–31it can be understood that,for the given combination of plasma-forming gas and etched material,the variations of etch rate versus main oper-ating parameters ͑gas pressure,gas flow rate,source power,and gas mixing ratios ͒depend on the volatility of reaction products ͑in fact,on the desorption mechanism for reaction products ͒and fluxes of active species on the etched surface.The low volatility of ZrCl x ͑Refs.5and 11͒allows one to neglect their spontaneous ͑thermally activated ͒desorption as well as to assume the ion-assisted chemical reaction to be the main etch mechanism,at least in the Cl 2-rich plasmas.Also,the direct chlorination of the ZrO 2surface at nearly room temperature seems to be impossible because the Zr–O bond is much stronger than the Zr–Cl one ͑8.06eV versus 5.11eV,respectively ͒.11That is why the role of ion bom-bardment includes,at least,͑1͒the destruction of the Zr–O bonds to support the formation of ZrCl x ,and ͑2͒the sputter-ing of the ZrCl x layer to provide the access of Cl atoms to the etched surface.In such a situation,the ion-flux-limited etch regime for the ZrO 2looks to be predetermined.For further investigations,we selected the gas mixing ratio as the main parameter and kept other parameters fixed.The reason is that the mixing ratio of Cl 2with Ar,He,or N 2directly reflects the transition between chemical and physical etch pathways and,thus,allows an accurate understanding of the etch mecha-nism.A.ZrO 2etch rateFrom Fig.1,it can be seen that an increase in fraction of any additive gas up to 80%results in the monotonic increase in the ZrO 2etch rate,which rises by a factor of 2.63in Cl 2/Ar plasma ͑1.20–3.15nm /min for 0%–80%Ar ͒,by a factor of 2.0in Cl 2/N 2plasma ͑1.20–2.40nm /min for 0%–80%N 2͒,and by a factor of 1.93in Cl 2/He plasma ͑1.20–2.31nm /min for 0%–80%He ͒.These situations are different compared with,for instance,the BCl 3/Ar plasma,where the addition of Ar resulted only in an insufficient change in the ZrO 2etch rate ͑35.8–31.4nm /min for 0%–83%Ar with a maximum of 41nm /min at 30%–35%Ar ͒.8For the BCl 3/He plasma,Ref.10reported an increase in the ZrO 2etch rate by a factor of 1.56͑36.2–56.7nm /min for 0%–83%He ͒,which is also lower than the results of the present work.Therefore,though Ar,He,and N 2are the inert gases with no direct chemical effects on the etch kinetics,their addition to Cl 2provides an evident acceleration of the ZrO 2etch process.From Fig.1͑b ͒,it can be seen that an increase in the ZrO 2etch rate is accompanied by a relatively weak decrease in the negative dc bias on the etched sample ͑−U dc =125–61,125–99,and 125–117for 0%–80%Ar,He,and N 2,respectively ͒.Considering that the sputtering yields Y for both native material and low volatile reactionproductsF IG .1.Measured ZrO 2etch rate ͑a ͒and negative dc bias ͑b ͒as functions of the additive gas fraction in the Cl 2/Ar,Cl 2/He,and Cl 2/N 2plasmas.The lines are to guide the eyes only.J.Vac.Sci.Technol.A,Vol.26,No.6,Nov/Dec 2008are proportional to the square root of ion bombardment en-ergy͑Refs.29and30͒͑andϷeU dc for the collisionlessplasma sheath͒,the changes in sputtering yields with increas-ing fraction of any additive gas can be assumed to be insuf-ficient.In pure Ar,the ZrO2etch rate͑in fact,the pure physi-cal sputtering rate͒is more than two times lower than that forpure Cl2plasma͑ϳ0.4nm/min͒while for pure N2and Hegases it is about0.2nm/min.Taking into account the in-creasing ion current densities for all three systems with in-creasing fractions of additive gases͑the corresponding datawill be discussed later͒,one can assume that a growth of theZrO2etch rate with additions of Ar,He,or N2up to80%israther connected with an acceleration of ion-assisted chemi-cal reaction than with increasing rate of physical sputteringof the native oxide surface.B.Plasma parameters and compositionFigure2illustrated the results of the LP plasma diagnos-tics.From Fig.2͑a͒,it can be seen that an increase in addi-tive gas fraction results in increasing electron temperatures inthe ranges2.16–2.67,2.16–7.46,and2.16–2.52eV for0%–80%Ar,He,and N2,respectively͓Fig.2͑a͔͒.The effect ofgas mixing ratio on T e results from the differences in thresh-old energies and cross sections for plasma components.Among Cl2,Cl,and additive gas species,the electron impactreactions for Ar,He,or N2have higher thresholds with closervalues of excitation and ionization potentials͑see Table I andRefs.10,22,and24͒,but lower cross sections at the EEDFmaximum.That is why the dilution of Cl2by the above-mentioned additive gas lowers the energy loss in the mediumpart of the EEDF,increases the fraction of“fast”electrons,and shifts T e toward higher values.22,24Figure2͑b͒showsthat an increase in the fraction of any additive gas from0%–80%causes a monotonic increase in measured n+,which arein the ranges8.82ϫ1010–3.71ϫ1011cm−3for Cl2/Ar, 8.82ϫ1010–1.18ϫ1011cm−3for Cl2/He,and8.82ϫ1010–9.64ϫ1010cm−3for Cl2/N2plasmas.This can be caused by an increase in total ionization rate as well as by thechange of total charge balance determining plasma quasineu-trality.Since the threshold energies for most of electron-impactprocesses exceed͑3/2͒T e,their rate coefficients are sensitiveto the change in gas mixing ratios and follow the behavior ofT e.In pure Cl2plasma,the effective rate coefficient for theformation of Cl atoms22,24͓k dis=͑k3+k4+2k5͒,where the low-case indices at k correspond to the reaction number inTable I͔is mainly contributed by R5͑Refs.21and22͒͑k5=6.47ϫ10−9–8.48ϫ10−9cm3/s for0%–80%Ar, 6.47ϫ10−9–1.57ϫ10−8cm3/s for0%–80%He,and 6.47ϫ10−9–8.18ϫ10−9cm3/s for0%–80%N2͒.Such a situa-tion is due to lower threshold of R5compared with R3and higher cross section compared with R3and R4providing k5/k3=2.18ϫ103,k5/k4=29,and k disϷ2k5.The dilution of Cl2by Ar,He,or N2does not change the situation except a bit decreasing k5/k3as well as increasing k5/k4.As the frac-tion of additive gas increases from0%–80%,an increase in the dissociation frequencydis=k dis n e͑1.76ϫ102–3.20ϫ103s−1for Cl2/Ar,1.76ϫ102–1.77ϫ103s−1for Cl2/He, and1.76ϫ102–6.67ϫ102s−1for Cl2/N2͒partially compen-sates a decrease in the Cl2density,so that the Cl atom for-mation rate falls slower than is predetermined by the change of the initial mixture composition.Accordingly,both density of Cl atoms n Cl and theirflux⌫ClϷ0.25n Cl͑8k B T/n Cl͒1/2 decrease only by factors of1.46,1.55,and1.71at60%Ar, He,and N2,respectively͓Fig.3͑a͔͒.An increase in the Cl2 dissociation degree͑n Cl/n Cl2=2.12–38.7, 2.12–21.3,and 2.12–8.05for0%–80%Ar,He,and N2,respectively͒is as-sociated with increasingdis.This result is in good agreement with published data.22,32,33Also,we obtain a not bad agree-ment in the relative behaviors of the model-predicted and measured by QMS Cl atom densities.The model-predicted electron density shows the same be-havior with n+and occupies the ranges2.63ϫ1010–3.67ϫ1011, 2.63ϫ1010–1.10ϫ1011,and 2.63ϫ1010–7.92 F IG. 2.Measured electron temperatures͑a͒and measured and model-predicted densities of charged species͑b͒as functions of the additive gas fraction in the Cl2/Ar,Cl2/He,and Cl2/N2plasmas.In͑a͒,the lines are to guide the eyes only.In͑b͒,the symbols are the measured n+,and the lines are the model predicted n e.JVST A-Vacuum,Surfaces,and Filmsϫ1010cm −3for 0%–80%Ar,He,and N 2,respectively ͓Fig.2͑b ͔͒.These correlate with a behavior of total ionization rates ͑5.53ϫ1014–6.63ϫ1015,5.53ϫ1014–1.34ϫ1016,and 5.53ϫ1014–8.72ϫ1014cm −3s −1for 0%–80%Ar,He,or N 2͒.The density of Cl −decreases from 6.19ϫ1010to 4.36ϫ109,from 7.2ϫ1010to 8.27ϫ109,and from 7.2ϫ1010to 1.49ϫ1010cm −3for 0%–80%Ar,He,or N 2,respectively ͑fol-lowing the rate of dissociative attachment R4͒,which corre-spond to n Cl −/n e =2.36–0.01, 2.36–0.08,and 2.36–0.19.These values are in good agreement with published data for low-pressure Cl 2and Cl 2/Ar ICPs.19–22In pure Cl 2plasma,the densities of Cl 2+and Cl +are quite close with n Cl +/n Cl 2+=0.85.The dilution of Cl 2by any additive gas increases the n Cl /n Cl 2ratio and causes the domination of Cl +over the Cl 2+providing n Cl +/n Cl 2+=1.40–13.4, 1.50–13.4,and 1.13–2.81for 20%–80%of Ar,He,or N 2,respectively.The density of Cl +was found to be higher than those for Ar +,He +,or N 2+even at 80%additive gas ͑n Cl +/n Ar +=1.6,n Cl +/n He +=220,and n Cl +/n N 2+=6.3͒.This is because of low ionization rates͑high threshold and low cross sections ͒for additive gas spe-cies.The flux of positive ions ⌫+͑which is mainly composed from Cl +͒,as well as the ion current density j is Х0.61e ͚n +,i i ,shows an increase with increasing additivegas fraction ͓Fig.3͑b ͔͒due to both n +and ion Bohm veloc-ity.An acceptable agreement between measured and model-predicted ion current densities allows one to assume that the models provide an adequate description of the steady-state gas phase composition and plasma parameters.C.Etch mechanism analysisFrom the above data,it can be understood that the behav-ior of the ZrO 2etch rate with increasing fractions of Ar,He,or N 2contradicts the behavior of ⌫Cl but follows the behav-ior of ⌫+.Such a situation is quite typical for the ion-flux-limited etch regime,which can be realized through both physical sputtering of the ZrO 2surface as well as through the ion-assisted chemical reaction with the ion-stimulated de-sorption of reaction products as the rate-limiting stage.Tak-ing into account the much lower ZrO 2etch rates in pure additive gases compared with those in pure Cl 2plasma,one can accept the last variant as the main reaction mechanism,at least under the given set of experimental conditions.To investigate the situation in detail,we applied the simplified model of etch kinetics for the ion-assisted chemical reaction,which is based on the theory of active surface sites.28–31Similarly to Refs.8–10,the assumptions were formulated as follows:͑1͒The Cl atoms are the main chemically active species,͑2͒the formation of low volatile Zr chlorides is the main channel for the loss of active surface sites,͑3͒the con-tribution of physical sputtering of ZrO 2can be neglected,and ͑4͒all types of positive ions are effective for the ion-stimulated desorption of reaction products.In such a situa-tion,the total etch rate is R Ϸ␦s 0⌫Cl ͑1−͒,where ␦is the stoichiometric coefficient for reaction products ͑for example,␦=0.25for ZrCl 4͒,s 0=0.3–0.5͑Refs.32–34͒is the sticking coefficient for etchant species,and is the fraction of chlo-rinated surface.When neglecting the spontaneous desorption of reaction products,the steady-state balance for free surfacesites ͑1−͒is ␦s 0⌫Cl ͑1−͒=Y d ⌫+,where Y d =A ͑1/2−01/2͒͑Refs.31and 32͒is the ion-type-averaged yield of ion-stimulated desorption,A is the constant,and 0is the desorp-tion threshold.The parameters A and 0for BCl 3plasma can be derived from the experimental dependence of ZrO 2etch rate on the incident ion energy as A =0.04–0.06and 0ϳ21eV ͑Y d ϳ0.5atom/ion for ϳ100eV ͒.5–7Considering that in our systems the dominant ion is Cl +instead of BCl 2+in the BCl 3plasma,the parameter A should be corrected pro-portionally to the momentum transferred to the surface in a single collision ͑i.e.,proportionally to ͱm i ͒.Finally,the rate of ion-assisted chemical reaction can be expressed as R =␦s 0⌫Cl ͩ1−␦s 0⌫Cl ␦s 0⌫Cl +Y d ⌫+ͪ.͑2͒For the given set of input parameters,and independently of the type of additive gas,one can obtain Y d ϳ0.5–0.4and ␦s 0⌫Cl /Y d ⌫+=70–5ӷ1for 0%–80%Ar,He,or N 2.This means that the efficiency of chlorination is higher than the efficiency of ion-stimulated desorption,the etched surface is highly chlorinated ͑=0.98–0.49͒,and a pure ion-flux-limited etch regime takes place,at least for 0%–50%additiveF IG parison of measured ͑symbols ͒and model-predicted ͑lines ͒Cl atom densities ͑a ͒and ion current densities ͑b ͒as functions of the additive gas fraction in the Cl 2/Ar,Cl 2/He,and Cl 2/N 2plasmas.J.Vac.Sci.Technol.A,Vol.26,No.6,Nov/Dec 2008gas.In such a situation,Eq.͑2͒can be simplified in a form of R ϷY d ⌫+showing that the etch is mostly sensitive to the change of Y d ⌫+and is weakly sensitive to the variations of ⌫Cl .The fact that the model-predicted etch rates ͑Fig.4͒do not reproduce the exponentlike increase of j is mentioned by Fig.3͑b ͒results from a decrease in the fraction of chlori-nated surface due to a decrease in ⌫Cl .Nevertheless,one can assume that the differences in the etch rates for various ad-ditive gases are mainly connected with the differences in charged species kinetics and transport.When the fraction of Cl 2in any gas mixtures reaches zero,we obtain ,R →0,and the etch rate is only the rate of physical sputtering,which is Y s ⌫+.The well known fact is that the sputtering yields Y s are normally much lower than the yields of ion-stimulated de-sorption ͑Y s ϳ0.05atom/ion for Ar +at ϳ100eV ͒.35This explains why the etch rate in pure Ar,He,or N 2gases is much lower compared with the Cl 2-containing mixtures.Also,the relative behaviors of the etch rates calculated using Eq.͑2͒are in not bad agreement with the experimental data.This allows one to assume that the model provides the ad-equate description of the main kinetic effects determining the behavior of the ZrO 2etch rate.Finally,we would like to note that the models of plasma chemistry and etch kinetics used in this work do not provide an exact quantitative analysis of the ZrO 2etching mechanism due to simplifications and some uncertainties in primary as-sumptions.However,the model-based analysis allows one to see the basic relationships between input process parameters and the etch rate,illustrates the relative contributions of both chemical and physical etch pathways,and determines the factors of primary influence on the process characteristics.IV.CONCLUSIONIn this work,we attempted the analysis of the ZrO 2etch kinetics and mechanisms using the Cl 2/Ar,Cl 2/He,andCl 2/N 2inductively coupled plasmas.It was found that an increase in any additive gas fraction causes an increase in the ZrO 2etch rate,which changes from 1.2nm /min for pure Cl 2plasma up to 3.15,2.40,and 2.31nm /min for 80%Ar,N 2,and He,ngmuir probe diagnostics and zero-dimensional plasma modeling showed that plasma param-eters,densities of active species,and their fluxes are sensi-tive to the fraction of additive gas,but the trends are the same for all three gas mixtures.It was found that,under the given set of experimental conditions,the ZrO 2etch rate is very low sensitive to the behavior of Cl atom flux and gen-erally follows the behavior of ion flux that corresponds to the ion-flux-limited etch regime of ion-assisted chemical reac-tion.In such a situation,the differences in the etch rates for various additive gases are mainly connected with the differ-ences in charged species kinetics and transport.1Ultrathin SiO 2and High-K Materials for ULSI Gate Dielectrics ,edited by H.R.Huff,C.A.Richter,M.L.Green,G.Lucovsky,and T.Hattori ͑Materials Research Society,Warrendale,PA,1999͒,V ol.567.2C.Chaneliere,J.L.Autran,R.A.Devine,and 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