螺杆式空气压缩机智能控制技术研究与应用

根据国家关于空气压缩机节能降耗及智能化控制要求,针对空气压缩机耗能运行现状、控制方式落后等问题,采用PID控制器、PLC智能控制、工业以太网等技术,设计了空气压缩机组智能控制系统。实现空压机组节能降耗、智能控制、远程监控、无人值守等功能,对于企业设备自动化化管理及经济安全运行具有重要意义。     

Radon and moisture impacts from interventions integrated with housing energy retrofits

Energy retrofits can reduce air exchange, raising the concern of whether indoor radon and moisture levels could increase. This pre/post-intervention study explored whether simple radon interventions implemented in conjunction with energy retrofits can prevent increases in radon and moisture levels. Treatment homes (n = 98) were matched with control (no energy retrofits or radon intervention) homes (n = 12). Control homes were matched by geographic location and foundation type. t-tests were used to determine whether post-energy retrofit radon and moisture level changes in treatment homes significantly differed from those in control homes. The radon interventions succeeded in preventing statistically significant increases in first floor radon using arithmetic (p = 0.749) and geometric means (p = 0.120). In basements, arithmetic (p = 0.060) and geometric (p = 0.092) mean radon levels statistically significantly increased, consistent with previous studies which found that basement radon levels may increase even if first floor levels remain unchanged. Changes in infiltration were related to changes in radon (p = 0.057 in basements; p = 0.066 on first floors). Only 58% of the change in infiltration was due to air sealing, with the rest due to weather changes. There was no statistically significant association between air sealing itself and radon levels on the first floor (p = 0.664). Moisture levels also did not significantly increase.     

低阶煤颗粒-气/油泡间的诱导时间研究

为表征低阶煤颗粒-气/油泡间矿化过程的差异,通过Sutherland理论下固体颗粒进入泡沫产品的总概率(E)和浮选速率常数(k)之间关系,并结合低阶煤颗粒-气/油泡的浮选速率试验,求得了低阶煤颗粒-气/油泡间的诱导时间。浮选实验研究表明,在相同的捕收剂消耗量下低阶煤-油泡浮选产率均高于低阶煤-气泡浮选产率。诱导时间测试表明,低阶煤颗粒-油泡间的诱导时间(35 ms)要明显低于低阶煤颗粒-气泡间的诱导时间(93 ms)。上述实验结果表明,油泡表面的疏水性要强于传统浮选气泡表面的疏水性。然而,进一步利用Sutherland理论中固体颗粒进入泡沫产品的总概率和浮选速率常数之间的数学关系,并结合低阶煤颗粒-气/油泡的浮选速率试验求得的低阶煤颗粒-气/油泡间的诱导时间分别为9.67和8.46 ms,其与诱导时间测试仪分别测量的诱导时间差异很大。这主要是由于在实际浮选过程中气/油泡的上升速度分别为23.26和22.68 cm/s,其远高于2015EZ型诱导时间仪测试过程中气/油泡碰撞速度(2.0 cm/s)。因此,诱导时间理论计算表明气泡-颗粒间的碰撞速度对颗粒-气泡间的诱导时间影响很大。上述研究结果表明油泡浮选效果优于传统浮选的内在原因在于低阶煤颗粒-油泡间的诱导时间小于低阶煤颗粒-气泡间的诱导时间。     

Analysis of color volume of multi‐chromatic displays using gamut rings

There are claims that multi‐chromatic displays can achieve a wider color gamut by the use of additional highly saturated secondary color channels. However, there are other claims that these displays lose lightness and/or color saturation at brighter levels. These apparently divergent views have led to some controversy in the display industry and at standard setting organizations. This study examines the color gamut volume for a variety of simulated and measured multi‐chromatic (sometimes incorrectly referred to as “multi‐primary”) displays using combinations of white and/or secondary color channels, such as cyan, magenta, and yellow. Furthermore, a two‐dimensional gamut representation, referred to as “gamut rings,” is introduced to illustrate that the addition of nonprimary optical color channels to a trichromatic (RGB) display can result in a significant decrease in the chroma at higher lightness levels. The additional saturated color channels can increase the gamut volume only around their hues at darker levels. The results also confirm the validity of comparing the color light output and white light output for revealing the design trade‐offs between the high‐peak white and the color‐image brightness for multi‐chromatic displays.     

助燃空气对乙烯裂解炉NOx排放的影响

乙烯裂解炉内复杂物理化学过程耦合模拟与优化能够满足乙烯装置对高效率、低污染和低成本的设计和操作要求，对提高乙烯工业的竞争力具有重要意义。针对简单燃烧机理难以准确预测炉膛燃烧生成NO_x浓度分布的弊端，提出了在裂解炉使用更准确的简化GRI-Mesh 3.0机理结合涡耗散概念(EDC)模型的方法，并对Sandia Flame D的燃烧过程进行计算流体力学(CFD)模拟，验证了此耦合模型的可靠性。在已建立的燃烧模型的基础上，研究了助燃空气对降低裂解炉NO排放的影响，结果表明：在满足裂解炉热效率的情况下，空气预热温度为300~600 K、过量空气系数为1.1时降低NO的效果最佳。     

基于永磁涡流传动的长距离带式输送机启动特性研究

针对矿用带式输送机启动过程易出现打滑、淤带和断带等问题,基于永磁涡流传动技术,将双盘式磁力耦合器作为带式输送机的驱动装置,建立双盘式磁力耦合器动态数学模型,运用AMEsim软件搭建带式输送机系统仿真模型,设置启动时间分别为60、80和100 s,采用Harrison控制曲线启动时,研究带式输送机满载启动时机头、机尾部输送带的速度特性和张力特性,张紧装置位移特性以及双盘式磁力耦合器调速气隙特性,仿真结果表明:当启动时间为60 s时,带式输送机输送带速度波动大,动张力明显,尾部输送带最大张力达到29 kN,启动过程不平稳;双盘式磁力耦合器调速时,气隙变化与带式输送机启动速度变化趋势相反,启动过程气隙从22 mm减小到4 mm;当启动时间为80 s和100 s时,带式输送机启动过程相对平稳,速度和张紧装置位移波动小,尾部输送带张力波动幅度分别为5 kN和3 kN;带式输送机启动过程存在最佳启动时间,继续延长时间,对带式输送机启动特性影响越来越小,80 s可作为合理启动时间。     

An iterative approach for the discrete‐time dynamic control of Markov jump linear systems with partial information

The , and mixed dynamic output feedback control of Markov jump linear systems in a partial observation context is studied through an iterative approach. By partial information, we mean that neither the state variable x(k) nor the Markov chain θ(k) are available to the controller. Instead, we assume that the controller relies only on an output y(k) and a measured variable coming from a detector that provides the only information of the Markov chain θ(k). To solve the problem, we resort to an iterative method that starts with a state‐feedback controller and solves at each iteration a linear matrix inequality optimization problem. It is shown that this iterative algorithm yields to a nonincreasing sequence of upper bound costs so that it converges to a minimum value. The effectiveness of the iterative procedure is illustrated by means of two examples in which the conservatism between the upper bounds and actual costs is significantly reduced.     

2 000 t/d水泥生产线烧成系统技术改造

为了解决烧成系统不稳定，操作控制困难，对煤质的适应性差，存在安全、环保隐患，系统能耗高等问题，在保留原预热器框架不变的情况下，加大了C1旋风筒上部直筒段及涡壳，重新设置了C2、C3、C4旋风筒导流板，重新设计了C5旋风筒涡壳，并改造了相应的连接风管和下料管，更换了锁风翻板阀和撒料箱。同时将带流化床的管道式离线分解炉改为在线喷旋管道式分解炉，并对三次风管进行了改造，三次风从分解炉锥部单股旋切引入。本次技术改造实现了原定的各项技改目标，取得了良好的节能降耗效果。     

综放工作面风量及采空区漏风定量检测

通过对中煤塔山煤矿30509综放工作面采空区漏风及有害气体分析的研究，总结了通过定量连续释放SF₆示踪气体，来检测工作面风量与采空区漏风的方法，测定了沿工作面采空区的漏风分布及漏风流线的深度。采用定时测量法，确定了30509工作面随工作面不断推进，与对应地表发生了导通现象；采用定量测量法，确定了内部漏风量和外部漏风量较大，对综采工作面采空区自然发火存在较大风险，同时提出了防范措施，为减少综放工作面采空区漏风、防止自然发火的发生提供了参考。     

新型“U”型板溶气气浮装置浓缩生化污泥的应用

介绍新型"U"型板溶气气浮装置以及"U"型板的工作原理,重点分析"U"型板溶气气浮对生化污泥的浓缩效果。在不同的污泥负荷、溶气回流比、PAC以及PAM加药量的情况下,进行气浮中试试验,寻找最佳的试验工况。试验结果表明,当污泥负荷为57 kg/(m^2·h)、溶气回流比为35%、PAC加药量为30 mg/L、PAM加药量为8 mg/L时,气浮出泥的污泥含固率能稳定在5.55%左右,"U"型板溶气气浮对生化污泥的浓缩效果很好。这对实际生产中气浮工艺取代二沉池以及重力浓缩池提供了现实可行的指导意义。