基于H4结构逆变器在不同调制方式下的性能比较

针对传统双极性调制和单极性调制方式在效率、总谐波失真THD(total harmonic distortion)以及电磁干扰等方面的问题,提出上慢下快调制方式和半周期工频半周期高频调制方式2种新控制策略。上慢下快调制方式在较高电压和电流上升率的工况下,对于驱动电路以及主电路中的杂散电感、电容的电磁干扰影响,能够有效抑制。半周期工频半周期高频调制方式在调制波(正弦波)过零点处无SPWM突变,有效改善输出电压过零点振荡的问题。在Matlab/Simulink仿真平台验证了4种调制方式的可行性。最后通过实验研究,结合效率、THD这2个参数进行对比分析,比较4种调制方式的性能,通过实验数据得出所提控制策略较传统调制方式在效率、总谐波含量以及电磁干扰等方面均有改善,证明了所提控制策略的可行性与有效性。     

铜冶炼企业产品质量控制的探索与实践

为了保持阴极铜化学成分和质量长期稳定,某铜冶炼企业对阴极铜化学成分进行监控,对铜冶炼生产系统中电解工序物料、产出后又重回本系统物料、贵金属系统中产出物料、外购原料中物料的杂质总量进行分析,提出了减少杂质对阴极铜质量影响的措施,为阴极铜质量的稳定创造了良好的生产条件,并提升了企业适应复杂原料市场的能力。     

水解-红外吸收光谱法测定精四氯化钛中总油

精四氯化钛是海绵钛及钛生产的关键原材料,提高海绵钛及钛质量的关键在于控制精四氯化钛中杂质含量。由于生产工艺原因,精四氯化钛中含碳杂质主要为油类杂质,因此测定精四氯化钛中油类杂质含量,对精四氯化钛中碳杂质的分析具有重要意义。总油以碳为主要成分,具有红外吸收带,因此能够利用红外吸收光谱法实现测定。而四氯化钛与水气接触极易发生水解反应,生成的氯化氢同样具有红外吸收峰,且氯化氢与油类的吸收峰波数较接近,致使氯化氢干扰红外吸收光谱法测定四氯化钛原样中总油含量。实验建立水解-红外吸收光谱法测定精四氯化钛中总油含量的方法,将四氯化钛样品与水按体积比1∶25水解平衡后,采用四氯乙烯萃取水解溶液中的总油,通过外标定量分析精四氯化钛中总油含量。校准曲线中总油的线性范围为0～80 mg/L,相关系数r为0.999 9;总油的检出限为2.5 mg/kg。方法用于测定3个精四氯化钛样品中总油,结果的相对标准偏差(RSD,n=6)为3.5%～4.1%;加标回收率为96%～109%。     

普碳钢超大总压下量可逆冷轧工艺技术及生产实践

针对目前我国部分钢企由于现有工艺装备投产较早、技术落后、机组能力不足，只能采取中间退火+二轧程工艺生产0.12～0.15 mm薄规格冷轧产品，生产成本增加、周转周期长，不能灵活应对复杂多变的冷轧市场需求的状况，开发了普碳钢单轧程可以实现95%以上超大总压下量的单机架六辊可逆冷轧机组。结合国内新投产的某1 150 mm单机架六辊可逆冷轧机组的稳定规模化生产实践，阐述了机组工艺设备选型、主要工艺技术参数配置和生产需解决的核心关键技术难点，同时列举了几种市场需求量大、附加值高的薄规格冷轧产品的现场实际生产工艺参数，以说明该机组的实际应用效果。     

城市地下工程自动导向测量系统

论述了城市地下工程自动导向测量系统 ,通过实例分析比较了该导向系统与地下水准和导线测量的精度和差异 ,得出一些有益的结论。     

氧化还原反应式配平中可能差错的几种情况

本文通过许多实例，指出了氧化还原反应式配平中可能出现的得失电子数不等或电荷数未配平、得失电子关系不对及反应式中酸碱性介质有错误等几种差错，并归纳了在酸碱性水溶液中平衡介质的方法。     

High solids content emulsions. III. Synthesis of concentrated latices by classic emulsion polymerization

Two different methods of producing bi‐ and trimodal latices of a mixture of methyl methacrylate, butyl acrylate, and small amounts of acrylic acid were tested. It is shown that a combination of concentrating blends of seed particles by semibatch reaction, followed by a nucleation of small particles plus a second semibatch phase allowed us to obtain stable latices with solids contents over 65% and viscosities of below 2500 mPa s^?1 with little coagulum formation. The key parameter in determining latex stability, coagulum formation, and viscosity appears to be the the particle size distribution, and especially its modification attributed to secondary nucleation. Because it is not possible to eliminate water‐soluble monomers from the polymerization recipe, secondary (homogeneous) nucleation must be minimized by careful addition of the free‐radical initiator and choice of monomer feed flow rates. The nucleation of the third population in the trimodal latices is best accomplished with a mixed surfactant system because renucleation by anionic surfactant alone leads to detrimental changes in the particle size distribution (PSD) resulting from excessive flocculation of particles. In addition, it was found that the viscosity of the final products was not sensitive to small changes in the ionic strength of the latex, although neutralization to a pH of 6 effectively doubles the final latex viscosity. © 2002 Wiley Periodicals, Inc. J Appl Polym Sci 84: 1916–1934, 2002; DOI 10.1002/app.10513     

色谱法分析煤气总硫

铂丝还原滴定法在测量干法脱硫后硫化物含量时，测量数据偏离实际结果，容易造成触媒中毒。提出了用气相色谱火焰光度检测器测定的方法，使数据更可靠、准确。     

Modelling a circulating fluidized bed riser reactor with gas—solids downflow at the wall

A predictive model was developed for the fully developed zone of a circulating fluidized bed (CFB) riser reactor operating in the fast fluidization regime that overcomes limitations of existing models. The model accounts for the upward flow of gas and solids in the core and downward flow of the two phases in the annulus. Additionally, a numerical solution methodology for the simulation of a riser reactor employing the hydrodynamic model was devised. A simulation was performed using the fast, main Claus reaction to demonstrate the effects of backmixing in the fast fluidization regime. It was found that the molar flow rates of the reactants leaving a fast fluidized CFB riser reactor were significantly higher than those leaving an identical reactor operating in the pneumatic transport regime.     

Dewatering of Sewage Sludge

Dewatering of sewage sludges is usually carried out using belt filter presses or centrifuges. The ability to remove water from sludges by mechanical dewatering is a property of both the sludge and the equipment used for dewatering. Newer high-solids centrifuges can remove more water than a belt press but require a higher chemical conditioning dose. The Gt value, the product of the mean velocity gradient and the shear time, has been found to be a useful parameter for characterizing the shear in mechanical dewatering equipment. Dewatering can be considered a two-step process, filtration followed by expression. The expression step is the most important of these and the benefits of various sludge processing techniques and conditioning chemical types remains a fruitful area of research.