网站大量收购独家精品文档,联系QQ:2885784924

[工学]30万吨年二甲醚装置分离工段工艺设计.doc

[工学]30万吨年二甲醚装置分离工段工艺设计.doc

  1. 1、本文档共46页,可阅读全部内容。
  2. 2、有哪些信誉好的足球投注网站(book118)网站文档一经付费(服务费),不意味着购买了该文档的版权,仅供个人/单位学习、研究之用,不得用于商业用途,未经授权,严禁复制、发行、汇编、翻译或者网络传播等,侵权必究。
  3. 3、本站所有内容均由合作方或网友上传,本站不对文档的完整性、权威性及其观点立场正确性做任何保证或承诺!文档内容仅供研究参考,付费前请自行鉴别。如您付费,意味着您自己接受本站规则且自行承担风险,本站不退款、不进行额外附加服务;查看《如何避免下载的几个坑》。如果您已付费下载过本站文档,您可以点击 这里二次下载
  4. 4、如文档侵犯商业秘密、侵犯著作权、侵犯人身权等,请点击“版权申诉”(推荐),也可以打举报电话:400-050-0827(电话支持时间:9:00-18:30)。
查看更多
[工学]30万吨年二甲醚装置分离工段工艺设计

3.0万吨/年二甲醚装置分离工段精馏塔设计 摘 要 二甲醚(DME)具有一系列优良的物理化学性质,可用于于制药、染料、农药、气溶胶喷雾剂和制冷剂,另外,二甲醚作为一种新型清洁能源,市场前景非常可观。所以对二甲醚生产工艺的研究具有重要意义。 本设计主要针对二甲醚生产工艺的分离工段进行计算。通过计算理论塔板数、塔效率、实际板数、进料位置,在板式塔主要工艺尺寸的设计计算中得出塔径、有效塔高、筛孔数。通过塔板的流体力学验算,证明各指标数据均符合标准,以保证精馏过程的顺利进行并使效率尽可能的提高。 二甲醚的分离是一个三组分的多组分分离,所以本设计采用两个简单精馏塔,即一个二甲醚塔和一个甲醇回收塔来将三种物质分离。为使工艺中尽可能的节约原料,所以将物系中的甲醇进行回收,继而将分离得到的甲醇气化得到气化甲醇,重新应用到生产流程中,使工艺流程更加合理化。 关键词:二甲醚 工艺设计 多组分分离 计算 Separation of Producing 30kt/a DME Process Design ABSTRACT Dimethyl ether (DME),which has many excellent physical and chemical properties for manufacturing pharmacy, dye, pesticide, spraying solvent and refrigerant, is widely used as raw materials. As a novel clean fuel, DME has a very promising future for developments. SO, it is magnificent to study on the process of producing DME. The design of the main production process for the separation of DME section in the calculation. Through the sieve plate distillation column design, I initial grasp the basic principles and methods of chemical design. Total condenser is used to accurately control the reflux ratio at the top of the tower, It use direct steam heating at Bottom of the column, in order to provide sufficient heat. By calculating the number of theoretical plates, efficiency, the actual plate number, feed location, it Calculate the column diameter, effective tower, sieve number by the main technical dimensions design calculation of Plate column. By checking fluid mechanics, it prove the index data are in line with standards, ensure the smooth progress and to improve efficiency as much as possible. Separation of DME is a separation of three components of the multi-component. Therefore, this design uses two simple distillation column, one of DME and one of methanol recovery. In order to process raw materials savings as much as possible, so the material in the methanol recovery system, and then the isolated methanol gasification gasified methanol, re-applied to the production process, so that process to rationalize. Keyword

文档评论(0)

ipbohn97 + 关注
实名认证
内容提供者

该用户很懒,什么也没介绍

1亿VIP精品文档

相关文档