首页> 外文会议>Annual International Pittsburgh Coal Conference (PCC) >CRYOGENIC METHOD OPERATING AT NORMAL PRESSURE AND BELOW FOR ENRICHING THE OXYGEN CONTENT IN AIR
【24h】

CRYOGENIC METHOD OPERATING AT NORMAL PRESSURE AND BELOW FOR ENRICHING THE OXYGEN CONTENT IN AIR

机译:在常压下及以下富集空气中氧气含量的低温法

获取原文
获取原文并翻译 | 示例

摘要

Oxygen and oxygen-enrichment are nowadays produced from air generally by threernmethods: cryogenic, adsorption and membrane separation. Various methods producerndifferent purities and mass flows of oxygen. Again, the utilization of oxygen-enrichment,rnI.e. not pure oxygen, is often sufficient in many combustion applications.rnThe process introduced in this paper is a novel cryogenic method producing oxygenenrichmentrnmore energy-efficiently than the methods used till now. The mass flow of thernproduced enrichment may vary with the number of parallel basic modules applied. Due tornthe low pressures used in the introduced process (at maximum approximately 1.3 bar abs.,rnabsolute pressure), the compression work needed is smaller than e.g. in the Linde-Fr?nklrnprocess (the maximum pressure about 6.5 bar abs.), and the process approaches tornreversible. Furthermore, the main fraction in mass flow of air, I.e. the nitrogen-enrichedrnfraction, is not liquefied which saves energy compared to the common cryogenic processesrnthat liquefy this fraction. Nevertheless, the achieved low temperature of the nitrogenenrichedrnfraction is efficiently utilized in pre-cooling of the incoming process air. Since thernprocess does not produce pure oxygen, the energy required to separate the last percents ofrnoxygen from nitrogen-enriched fraction is saved. This is noticeable because of the lastrnpercents demand proportionately most separation energy.rnMoreover, the core of the process concerned consists of two nested columns that have arnheat exchange interaction with each other on their entire lengths. The adiabaticrnrectification columns used commonly nowadays only have a partial heat exchange contact,rnrespectively. Thus, the applied construction is both simple and thermodynamicallyrneconomical. Since the prevailing pressure is kept different on the various sides of the mainrnheat exchange surface, I.e. both the nested columns have different pressures, the phasernchange of the produced fraction occurs at different temperatures in the various columns.rnConsequently, the other main power source needed to maintain the process in operation isrnan air pump for compressing the low pressure product gas from the evaporation (inner)rncolumn to atmospheric pressure. The other power source is needed to feed in air into thernprocess.rnIn this paper, the novel cryogenic method operating at normal pressure and below it forrnproducing oxygen-enrichment is introduced. The theory behind the process as well as somernmodeling and experimental results are studied.
机译:如今,氧气和富氧通常是通过三种方法从空气中产生的:低温,吸附和膜分离。各种方法产生的氧气纯度和流量不同。再次,利用氧气富集。在许多燃烧应用中,通常不使用纯氧就足够了。本文介绍的方法是一种新型的低温方法,它比目前使用的方法更能节能地产生氧气。所产生的浓缩物的质量流量可能会随所应用的平行基本模块的数量而变化。由于在引入过程中使用的低压(最大绝对压力约为1.3巴,绝对值),因此所需的压缩功小于例如0.5MPa。在Linde-Fr?nklrn过程中(最大压力约为6.5 bar abs。),该过程接近可逆的。此外,空气质量流量的主要部分,即与液化该馏分的普通低温过程相比,富氮馏分没有被液化,从而节省了能量。然而,在进入的工艺空气的预冷却中,有效利用了氮富集馏分的低温。由于该过程不会产生纯氧,因此可以节省从富氮馏分中分离出最后百分之一的氧所需的能量。这是很明显的,因为最后一个百分数要求最大的分离能量。此外,该过程的核心由两个嵌套的塔组成,这些塔在整个长度上相互之间具有热量交换相互作用。当今常用的绝热精馏塔分别仅具有部分热交换接触。因此,所应用的构造既简单又热力学上经济。由于在主热交换表面的各侧保持主导压力不同,即两个嵌套塔都具有不同的压力,在不同的塔中,所产生馏分的相变在不同的温度下发生。因此,维持该过程运行所需的另一个主要动力来源是南空气泵,该空气泵用于压缩来自蒸发的低压产物气(内)柱至大气压。本文还介绍了一种新的低温方法,该方法在常压下工作并在低于常压的条件下产生氧气富集。研究了该过程背后的理论,以及一些建模和实验结果。

著录项

  • 来源
  • 会议地点 Osaka(JP)
  • 作者单位

    Institute of Energy and Process Engineering, Tampere University of Technology, P.O.rnBOX 589, FIN-33101 Tampere, Finland, Stanford University, Stanford, CA 94305-3032, USA, tel. +1-650-725 0915, fax +1-650-723 1748 Emails:rnilkka.saarenpaa@tut.fi;

    Institute of Energy and Process Engineering, Tampere University of Technology, P.O. BOX 589, FIN-33101 Tampere, Finland, tel. +358 3 311 511, fax +358 3 3115 3751, Emails:hanna.knuutila@tut.fi;

    Institute of Energy and Process Engineering, Tampere University of Technology, P.O.BOX 589, FIN-33101 Tampere, Finland, tel. +358 3 311 511, fax +358 3 3115 3751,Emails:pauli.haukka@tut.fi;

  • 会议组织
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号