基于PR控制器的APF电流跟踪控制策略研究

分析了基于同步谐波旋转坐标系下的电流跟踪控制策略,研究基于PR控制器的静止坐标系下的电流控制方法。理想的PR控制器在谐振频率下增益为无穷大,可以实现谐振频率相同的正弦信号无静差控制。因此,在PI控制的基础上通过分析并联谐振控制器,实现对特定次谐波进行重点补偿。     

具有内模结构的锅炉汽包水位PID控制

锅炉是向诸多工业生产过程提供热能与动力的重要设备之一.为了有效地克服汽包水位的负调现象,采用一种基于三冲量控制方案的内模PID控制方法,即副回路利用常规PI控制算法快速抑制给水流量变化带来的干扰,主回路采用内模PID控制算法用以克服蒸汽流量变化产生的扰动.仿真结果表明所提出的控制策略能够加快响应,减小超调,缩短调节时间,算法简单易于工程实现且具有较强的鲁棒性.     

单片微机在交流励磁机旋转整流器故障检测方面的应用

本文采用单片微机在软件上对交流励磁机旋转整流器故障信号进行频域分析,从中检测出旋转整流器的各类故障.     

轮胎成型机旋转密封技术研究

在经济全球化的背景下,随着我国轮胎生产技术的提高,轮胎企业和世界汽车工业的迅猛发展,我国轮胎的生产量不断增加.近年来,随着轮胎生产技术不断提高,轮胎成型机科技成果不断涌现,消费者对于轮胎的耐用性、安全性、舒适度和环保方面更加优质的产品的需求不断增加.本文对轮胎成型机旋转密封的结构、系统稳定性以及使用寿命进行简单介绍,讨...     

Modelling of copper etching in aerated chloride solutions

The effect of dissolved oxygen on the rate of chemical etching of copper by acidic cuprous chloride solution was investigated numerically for the case of a rotating disc electrode (RDE). Copper dissolution in aerated acidic cupric chloride solutions of composition 3.5M CuCl2 + 0.5M HCl + 0.5M KCl and 3.5M CuCl2+0.5M HCl was investigated with consideration of the instantaneous homogeneous reaction 4CuCl32-+4H++O2rlhar4CuCl 3-+2H2O which takes place within the mass transport boundary layer. It was assumed that CuCl32- and O2 react instantaneously, resulting in the formation of a reaction plane which separated the mass transport boundary layer into two regions: a region adjacent to the electrode where oxygen was depleted, and a region adjacent to the bulk where CuCl32- was absent. A one-dimensional mathematical model was developed to predict the position of the reaction plane. The model accounted for diffusion, migration and fluid flow generated by an RDE and included nine species and five heterogeneous electrochemical reactions. The homogeneous redox reaction served to regenerate the chemical etchant solution and thus enhance the etch rate. With increasing oxygen concentration and rotation rate the reaction plane was found to move closer toward the electrode and thus the etch rate of copper increased. Addition of KCl increased the Cl- content in solution so as to shift the reaction plane toward the bulk.     

网板填料复合旋转床的流体力学与传质性能

开发了一种新型的气液接触设备——网板填料复合旋转床。常压下以空气-水物系和乙醇-水物系在网板填料复合旋转床中进行流体力学与传质性能实验,考察了气液流量和转子转速对网板填料复合旋转床压降和传质性能的影响。实验结果表明,气体流量和转子转速的增大均使干、湿床气相压降增大;液体流量的增加对湿床压降的影响不明显。回流量和转速的增加均使等板高度减少至一定值后几乎不变。网板填料复合旋转床具有通量大、效率高、压降小的特点。     

2种防腐工艺技术在长庆油田的应用

简述了传统环氧酚醛清漆浸涂技术和高速旋转喷涂技术的工艺原理,工艺流程、以及2种技术处理的油管在中国石油长庆油田公司的应用现状。结合实验室评价结果和具体案例,综合对比了2种工艺的使用效果,为评价2种工艺的差别提供了必要的支持,对长庆油田今后选择和确定防腐油管类型也有一定的指导意义。     

滚筒现场冷硫化包胶技术在顾桥选煤厂的应用

对选煤厂内带式输送机滚筒包胶的作用及技术要求进行详细说明,指出了滚筒包胶在皮带机运行中的重要性。通过对传统的滚筒热硫化包胶工艺及现场冷硫化包胶工艺进行分析,指出传统热硫化包胶技术在事故应急处理、原材料选用、包胶工艺及使用效果等方面存在的不足。通过对比发现:现场冷硫化包胶技术在相同情况下原材料使用寿命长,使用效果好,操作方便。并介绍了德国TIP TOP公司开发的滚筒现场冷包胶技术,通过在顾桥选煤厂实际应用,证明了滚筒现场冷硫化包胶技术具有操作方便、使用效果好等优点,非常适用于选煤厂、井下等作业环境较差的地方。     

Improved gas holdup in novel bubble column

This investigation reports the experimental and theoretical results carried out to evaluate the gas holdup for air–water system in a novel hybrid rotating and reciprocating perforated plate bubble column under countercurrent condition. The response of this hybrid column is found to be similar to that of reciprocating plate column (RPC) showing mixer‐settler, transition, and emulsion regions. The effect of agitation level, superficial gas velocity, superficial liquid velocity, perforation diameter, and plate spacing on gas holdup is studied and found to be significant. The gas holdup is found to be least in the range of agitation level of 1.3–1.5 cm/s. For all the superficial gas and liquid velocities considered in this present investigation, the critical agitation level at minimum gas holdup remains nearly same. The gas holdup in this hybrid column is 1.2–1.7 times higher in mixer‐settler region and 2.1–2.7 times higher in emulsion region than that of RPC. Correlations have been developed and found to concur with the experimental values. It can be used with 95% accuracy. © 2011 Canadian Society for Chemical Engineering     

Gas‐Liquid Mass Transfer Characteristics in a Rotating‐Drum Bioreactor

The oxygen volumetric mass transfer coefficient is a key parameter to characterize the performance of aerobic bioreactors. A novel rotating‐drum bioreactor (RDB) fitted with a sparger as proposed in a previous work has demonstrated its excellent gas‐liquid mass transfer performance. To provide primary information on the design and scale‐up of the novel RDB, effects of reactor configuration including the number and width of lifters and operation conditions such as rotational speed, aeration rate, and solid volume fraction on mass transfer performance were systematically investigated in a new medium‐sized RDB. Compared with the stirred bioreactor and traditional RDBs, this new RDB exhibits better mass transfer performance. Taking both operational and reactor configuration parameters into consideration, an empirical correlation to predict the volumetric mass transfer coefficient in this type of RDBs was proposed which is valuable for its design and scale‐up.