ImageVerifierCode 换一换
格式:DOCX , 页数:4 ,大小:81.91KB ,
资源ID:7337496      下载积分:3 金币
快捷下载
登录下载
邮箱/手机:
温馨提示:
快捷下载时,用户名和密码都是您填写的邮箱或者手机号,方便查询和重复下载(系统自动生成)。 如填写123,账号就是123,密码也是123。
特别说明:
请自助下载,系统不会自动发送文件的哦; 如果您已付费,想二次下载,请登录后访问:我的下载记录
支付方式: 支付宝    微信支付   
验证码:   换一换

加入VIP,免费下载
 

温馨提示:由于个人手机设置不同,如果发现不能下载,请复制以下地址【https://www.bdocx.com/down/7337496.html】到电脑端继续下载(重复下载不扣费)。

已注册用户请登录:
账号:
密码:
验证码:   换一换
  忘记密码?
三方登录: 微信登录   QQ登录  

下载须知

1: 本站所有资源如无特殊说明,都需要本地电脑安装OFFICE2007和PDF阅读器。
2: 试题试卷类文档,如果标题没有明确说明有答案则都视为没有答案,请知晓。
3: 文件的所有权益归上传用户所有。
4. 未经权益所有人同意不得将文件中的内容挪作商业或盈利用途。
5. 本站仅提供交流平台,并不能对任何下载内容负责。
6. 下载文件中如有侵权或不适当内容,请与我们联系,我们立即纠正。
7. 本站不保证下载资源的准确性、安全性和完整性, 同时也不承担用户因使用这些下载资源对自己和他人造成任何形式的伤害或损失。

版权提示 | 免责声明

本文(化学反应工程作业.docx)为本站会员(b****6)主动上传,冰豆网仅提供信息存储空间,仅对用户上传内容的表现方式做保护处理,对上载内容本身不做任何修改或编辑。 若此文所含内容侵犯了您的版权或隐私,请立即通知冰豆网(发送邮件至service@bdocx.com或直接QQ联系客服),我们立即给予删除!

化学反应工程作业.docx

1、化学反应工程作业The Final Examination ofChemical Reaction Engineering Used by graduate students of 2010 2011-6 Name: Class: Grade: Student Number:1: For a gas reaction at 400 K the rate is reported as (a)What are the units of the rate constant?(b)What is the value of the rate constant for this reaction if t

2、he rate equation is expressed as 2: For the elementary reactions in seriesfind the maximum concentration of R and when it is reached.3: Given a gaseous feed, T0=1000 K, 0=5 atm, CA0=100, CB0=200, T=400 K, =4 atm, CA=20. Find XA, XB, CB.4: A gaseous feed of pure A (1 mol/liter) enters a mixed flow re

3、actor (2 liters) and reacts as follows: Find what feed rate (liter/min) will give an outlet concentration CA=0.5mol/lliter.5: The kinetics of the aqueous-phase decomposition of A is investigated in two mixed flow reactors in series, the second having twice the volume of the first reactor. At steady

4、state with a feed concentration of 1mol A/liter and mean residence time of 96 sec in the first reactor, the concentration in the first reactor is 0.5 mol A/liter and in the second is 0.25 mol A/liter.Find the kinetic equation for the decomposition.6: T is the desired product and CA0=5.Under ultravio

5、let radiation, reactant A of CA0=10 kmol/m3 in a process stream (v=lm3/min) decomposes as follows.We wish to design a reactor setup for a specific duty. Sketch the scheme selected, and calculate the fraction of feed transformed into desired product as well as the volume of reactor needed.7: When oxy

6、gen is bubbled through a high-temperature batch of A-containing liquid material, A oxidizes slowly to give a slowly decomposing intermediate X and final product R. Here are the results of an experiment:We have no way of analyzing for X; however, we are safe in assuming that at any time CA+CR+CX=CA0.

7、What can we say about the mechanism and kinetics of this oxidation? Hint: plot the data and examine the plot.8: Phthalic Anhydride from Naphthalene. The accepted mechanism for the highly exothermic solid catalyzed oxidation of naphthalene to produce phthalic anhydride isand whereA=naphthalene (react

8、ant)R=naphthaquinone (postulated intermediate)S=phthalic anhydride (desired product)T=CO2+H2O (waste products)and the Arrenhius activation energy is given in units of J/mol. This reaction is to be run somewhere between 900 K and 1200 K.A local optimum reactor setup discovered by the computer see exa

9、mple1, Chem. Eng. Sci., 49, 1037-1051(1994) l is shown in Fig.P10.19.Figure P10.19(a) Do you like this design? Could you do better? If so, how ?(b)If you could keep the whole of your reactors at whatever temperature and 7 value desired, and if recyle is allowed, how much phthalic anhydride could be produced per mole of naphthalene reacted?Suggestion: Why not determine the values of k1, k2, k3,and k4, for both extremes of temperature, look at the values, and then proceed with the solution?

copyright@ 2008-2022 冰豆网网站版权所有

经营许可证编号:鄂ICP备2022015515号-1