微型化学实验反应器设计

介绍了几种微型化学实验反应器的设计和使用方法，供同行参考。     

Flow Field of Circulating Fluidized Bed Reactor with Venturi Inlet Configuration

Different two-equation k-ε models were used to simulate the gas flow field generated by a new type of circulating fluidized bed reactor with venturi gas distributor. The numerical results were compared with the experimental data. It has been shown that the simulation results from the standard k-ε model have the best match with the experimental data. Based on this model, the gas flow field in the venturi diffuser and riser was analyzed by the concept of velocity nonuniformity and dead zone percentage. Both the nonuniformity of gas velocity and the dead zone percentage reach the maximum at the venturi outlet due to the effect of the vortex. At the same time, it provides a good platform for the further optimization of the inlet configuration of circulating fluidized bed reactor.     

发酵产氢的影响因素Ⅱ.反应器类型、营养条件和环境条件

发酵产氢技术在国内外受到了普遍关注,然该过程是一个极其复杂的生物过程,受诸多因素的干扰.如何优化产氢过程,确保稳定、持续和高效的产氢能力已成为发酵产氢研究的重点课题.本文在查阅了国内外大量文献的基础上,总结了主要影响因子(包括接种物、基质、反应器类型、营养条件和环境条件)对发酵产氢的影响,对发酵产氢朱朱的研发工作提出了...     

谐波对电容的影响及防范措施

简要介绍了电力系统中谐波对电容器造成的影响及原因,以及理论上的解决方法,并结合实际提出了解决谐波影响的实施措施。     

高职反应器的选型与操作课程开发

以校企合作为契机,开发符合高职教育特点的以职业岗位工作过程为导向的项目化课程——反应器的选型与操作,该课程以学生为主体,以职业能力培养为本位,以实践为主线,大大提升了学生的职业素养。本文在课程目标、课程内容的组织与序化、教学模式、教学方法和手段以及考核体系等方面做了详细阐述。     

节能搅拌反应器的应用

针对发酵有机酸在中和、酸解过程中出现混合不均匀、能耗大、蛄垢严重的问题,通过设备使用、工艺过程检测和分析,找出了存在问题的原因.对反应器、搅拌装置重新设计,提高反应器内壁及搅拌器的加工精度,经使用验证,提高了产品质量和生产效率,降低能耗和装置结垢现象,提高了公司经济效益.     

第二脱氢反应器设计及制造技术方案

苯乙烯装置的核心设备是苯乙烯第一、第二脱氢反应器,采用的是进口设备,已经使用15年,出现了苯乙烯流出量不够及填料支持强度不足问题。文章分析了第二脱氢反应器的结构特点、工作原理、操作工艺流程等,通过计算,提出了第二脱氢反应器替代进口设备的设计、制造技术方案。     

基于技术轨道结构理论的核电堆型技术演变与我国的选择

核电堆型技术的创新沿着轨道内和轨道间的两种结构方向发展:在单一堆型轨道内,以顺轨式累积型创新产生技术性能多样化的机型;在多堆型轨道间,以跃轨式革命型创新发生堆型的转换,或以融轨式集成型创新形成新堆型。我国需统筹核电堆型的发展:形成压水堆自主品牌系列,加快第四代核电堆型的商用进程,研发战略性新堆型。     

顺酐生产工艺与反应器研究进展

阐述了苯氧化法、C4烯烃氧化法、正丁烷氧化法生产顺酐的工艺过程及特点,综述了顺酐生产反应器的要求及类型,展望了顺酐生产工艺与反应器的发展方向。     

Investigation on the application of reformed coke oven gas in direct reduction iron production with a mathematical model

To investigate the application of reformed coke oven gas （COG） in producing the direct reduction iron （DRI）, we simulated a countercurrent gas solid moving bed reactor in which the iron ore pellet was reduced by reformed COG. An ordinary differential equation （ODE） was set based on the unreacted shrinking core model considering both mass and energy balances of the reactor. The concentration and temperature profiles of all species within the reactor were obtained by solving the ODE sys tem. The solid conversion and gas utilization were studied by changing gas flow rate, solid flow rate, reactor length, and the ratio of O/CHa to guide the practical application of COG in DRI production. Model results showed that COG was suitable for the DRI production. In order to meet the requirement of the industrial production, the minimum gas flow rate was set as 130,000 Nm3/h, and the maximum production was 90 t/h. The reactor length and the mole ratio x（O）： x（CH4） were depended on the actual industrial situations.