2006～2007年世界塑料工业进展

收集了2006年7月～2007年6月世界塑料工业的相关资料,介绍了2006～2007年世界塑料工业的发展情况,提供了世界塑料产量、消费量及全球各类树脂的需求量及产能情况.按通用热塑性树脂(聚乙烯、聚丙烯、聚苯乙烯、聚氯乙烯、ABS树脂)、工程塑料(尼龙、聚碳酸酯、聚甲醛、热塑性聚酯、聚苯醚)、特种工程塑料(聚苯硫醚、液晶聚合物、聚醚醚酮)、通用热固性树脂(酚醛、聚氨酯、不饱和聚酯树脂、环氧树脂)不同品种的顺序,对树脂的产量、消费量、供需状况及合成工艺、产品应用开发、树脂品种的延伸及应用的进一步扩展等技术作了详细介绍.     

知识创新是工业尿素合成技术创新之本——实验室研究篇

对国内外研究者在尿素合成反应的热力学、动力学、化学平衡及相平衡等方面的研究成果进行了总结和评价,提供了尿素合成反应的热力学、动力学数据和相图,提出了一些新理念.     

意大利ES公司变频器进入中国市场

3月11日,"意科走进中国"新闻发布会在京举行,与来自冶金、石化、电力、建材、水处理、纺织、市政等行业的专家、用户及十几家业内知名的媒体共同分享了意科公司的发展历程,意科变频器的创新标准以及意科在奥运年全面推向中国市场的决心和计划.     

中国工程塑料市场综述(下)

4.3 聚碳酸酯海关进出口分析 1999～2006年间PC进口量年均增长27.91%,比1998～2005年间PC进口量年均增长率31.27%下降3.36个百分点.国内产量偏低、市场需求巨大的现状进一步暴露.中国PC消费主要依靠进口,2006年中国产量仅占总消费量的10%上下.1999～2006年间PC进口量年均增长27.91%,比1998～2005年间Pc进口量年均增长率36.68%下降3.36个百分点.2006年初级形状的聚碳酸酯进口地有45个,主要进口地为泰国(占16.49%),其次为中国(12.86%)、新加坡(11.50%)、美国(10.95%)、日本(10.65%)、韩国(9.81%)、中国台湾省(9.50%)、西班牙(7.46%),八进口地进口量占总进口量的89.2%.     

夹层粘接在大型机床导轨修理中的应用

1 "夹层粘接"新工艺 "夹层粘接"是作者经多年研究、开发的一种新技术,在设备大修理工作中,对于严重摩擦磨损的机床导轨,采用独特的"夹层粘接"工艺,以夹布塑料为加厚层,填充F4为表面耐磨层,使机床导轨恢复了原有的精度和尺寸要求,缩短了修理时间,减轻了劳动强度,节约了修理费用,取得了显著的综合效益.     

加压稀硝"三合一"主机修理小结

我公司年产80 kt加压稀硝装置是国内首例完全国产化装置,其"三合一"主机的汽轮机、减速机由杭汽制造,空压机、膨胀机由陕鼓生产.自1986年装置建成投运以来,每年检修都发现机组气封严重磨损,机壳与转子不同心.为此,公司利用2006年11月大修和2007年7月停车机会对机组进行了全面整修,以期从根本上消除存在的问题.     

工业评述2001～2002年国外塑料工业进展

收集了2001年7月到2002年6月有关国外塑料工业的相关期刊资料,介绍了2001年到2002年国外塑料工业的发展情况,提供了世界各地域塑料原材料的产量及构成比,日本、美国、加拿大、德国、法国、比利时、墨西哥、芬兰、西班牙等国家的树脂产量、消费量及增长率,以及日本、西欧、北美等地区的不同品种塑料原料消费量和增长率统计.按通用热塑性树脂(聚乙烯、聚丙烯、聚苯乙烯、聚氯乙烯、ABS树脂)、工程塑料(尼龙、聚碳酸酯、聚甲醛、热塑性聚酯、聚苯醚)、通用热固性树脂(酚醛、聚氨酯、不饱和树脂、环氧树脂)、特种工程塑料(聚苯硫醚、液晶聚合物、聚醚醚酮)不同品种的顺序,对树脂的产量、消费量及合成工艺、产品应用开发、树脂品种的延伸及应用的进一步扩展等有关技术作了详细的介绍.     

骨胶生产中蒸骨制胶操作方法

1 对蒸骨制胶过程的认识 蒸骨制胶的过程也就是用蒸汽使骨料块在密封的锅内受热、受压,使骨质疏松,由生胶质热解转变为可溶解于热水的动物胶质(习惯上称之为"骨胶")的过程.     

合成TBHQ的工艺改进

研究了以工业品甲基叔丁基醚(MTBE)和对苯二酚(HQ)为原料,在磷酸催化下,合成TBHQ的工艺参数.对催化剂的活性、原料的配比和反应时间等进行了优化考察.当对苯二酚∶甲基叔丁基醚∶磷酸=1∶1∶0.5(mol),反应温度为125℃,反应时间3.5h,TBHQ的收率达85.7%.与传统方法相比,该方法具有价廉、操作简单的特点,具有较高的开发、应用价值.用MTBE作原料合成TBHQ未见有关文献具体报道.     

湖光山色清新隽永——访江西省高级工艺美术师杨修勇

在我的办公桌上,放着一把<井岗山八角楼>粉彩山水壶,每当我空闲时,总喜欢拿在手中把玩,这件小小的山水壶虽不能展现气势豪雄的大写意山水画面,也不可能真正达到烟云满纸的效果,但细腻的工笔,雅静的画意给人一种清心的感觉和享受.     

On-line multivariable adaptive control of a binary distillation column

An experimental evaluation of the simultaneous control of top and bottom product compositions of a binary distillation column utilizing multi-variable self-tuning control algorithms is presented. The study was carried out using an 8-tray, 22.86 cm diameter methanol–water pilot scale column with continuous capacitance analysis of top product composition and bottom composition analyzed on a 3 minute cycle, by a gas chromatograph. Column control is studied for ±25% step disturbances in feed flow rate. Terminal composition regulation using both ‘positional’ and ‘incremental’ forms of a generalized minimum variance self-tuning control algorithm is compared with that achieved using a conventional digital PI/PID multiloop control strategy.     

裂解炉的先进控制

介绍了中国石油大庆石化公司化工一厂乙烯装置GK一Ⅵ型裂解炉的主要控制方案，并结合工艺操作具体说明控制方案的实现过程。     

NONLINEAR MODEL PREDICTIVE CONTROL

Nonlinear Model Predictive Control (NMPC), a strategy for constrained, feedback control of nonlinear processes, has been developed. The algorithm uses a simultaneous solution and optimization approach to determine the open-loop optimal manipulated variable trajectory at each sampling instant. Feedback is incorporated via an estimator, which uses process measurements to infer unmeasured state and disturbance values. These are used by the controller to determine the future optimal control policy. This scheme can be used to control processes described by different kinds of models, such as nonlinear ordinary differential/algebraic equations, partial differential/algebraic equations, integra-differential equations and delay equations. The advantages of the proposed NMPC scheme are demonstrated with the start-up of a non-isothermal, non-adiabatic CSTR with an irreversible, first-order reaction. The set-point corresponds to an open-loop unstable steady state. Comparisons have been made with controllers designed using (1) nonlinear variable transformations, (2) a linear controller tuned using the internal model control approach, and (3) open-loop optimal control. NMPC was able to bring the controlled variable to its set-point quickly and smoothly from a wide variety of initial conditions. Unlike the other controllers, NMPC dealt with constraints in an explicit manner without any degradation in the quality of control. NMPC also demonstrated superior performance in the presence of a moderate amount of error in the model parameters, and the process was brought to its set-point without steady-state offset.     

模糊控制的现状与工程应用关键问题研究

详细阐述了模糊控制技术的研究现状,包括经典模糊控制、智能模糊控制和复合模糊控制。研究分析了模糊控制技术在工程应用中存在的若干问题,包括模糊控制规则和参数优化问题、强耦合多变量问题和模糊控制稳态精度问题,并根据目前国内外模糊控制技术的研究趋势,指出了模糊控制技术未来的研究方向。     

Generic model control — A case study

This paper outlines the use of a process model directly in a control algorithm. The process considered, a forced circulation single-stage evaporator, is a nonlinear interacting process. The control strategy employing a process model derived from fundamental mass and energy balances is shown to outperform single loop and predictive control strategies by a significant amount. The control structure is first presented in general form and then specifically applied to this process.     

Two-degree-of-freedom output feedback controllers for discrete-time nonlinear systems

A discrete-time, model-based output feedback control structure for nonlinear processes is developed in the present work. The structure makes use of a closed-loop observer, while at the same time it guarantees that the overall feedback controller possesses integral action. An algebraic transformation is applied on the observer states to insure that the input/output gain of the observer matches the model upon which the static state feedback control law is based. The resulting control algorithm is a two-degree-of-freedom control law, in the sense that the output and the set point are processed in different ways. The control structure is shown not only to have the same properties as the standard model-state feedback structure, but also that it emerges from a model algorithmic control framework. Finally, a simulation example using an exothermic CSTR operating at an open-loop unstable steady state is used to evaluate the closed-loop performance of the proposed method.     

Two-degree-of-freedom output feedback controllers for nonlinear processes

In this work, a nonlinear output feedback control algorithm is proposed, in the spirit of model-state feedback control. The structure provides state estimates using a process model, the measured output, and the residual between the model output and the measured output. These estimates will track the process states at a rate determined by a set of tunable parameters. An algebraic transformation of the state estimates is incorporated in the control structure to ensure that the input/output gain of the observer matches the model upon which the static state feedback control law is based. The transformed states are then used in the control law. This leads to a controller of minimal order possessing integral action. The control structure is shown to have the same properties as the standard model-state feedback structure. The resulting algorithm is a two-degree of freedom control law, in the sense that the control action is not a function of the error only, but the output and the set point are processed in different ways. Finally, a simulation example using an exothermic CSTR operating at an open-loop unstable steady state is used to demonstrate the closed-loop performance of the proposed method.     

轮胎硫化生产过程的模糊控制

分析轮胎硫化生产过程的特点,建立了硫化罐温度和压力控制的多维模糊控制数学模型,设计了适合该模型的控制算法,并在实际工程中予以实现。实践表明该控制方法具有较好的鲁棒性和较好的控制效果,并具有一定的推广价值。     

Generic model control — A case study revisited

The application of the Generic Model Control (GMC) algorithm to the control of an evaporator has been reported recently by Lee et al. (1989). The results of their case study are claimed to demonstrate the superiority of the nonlinear GMC algorithm over conventional techniques including Dynamic Matrix Control. In this note it is shown that for the evaporator example the improved performance arises primarily from the full multivariable and feedforward nature of the control law, rather than from the nonlinear nature of GMC.     

大时滞过程中的智能复合控制方法及应用

针对复杂工业过程中通常存在的大时滞现象,本文介绍了几种智能复合控制方法,并对其应用进行举例说明。