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纸机干燥部结构形式探讨 总被引:4,自引:2,他引:2
我国目前的中速和高速纸机,干燥部多采用单排烘缸排列型式。这种型式占地面积大、建筑投资费用高,实用上存在诸多局限性。未来,现代化的中速和高速纸机,干燥部的发展方向仍以蒸汽烘缸干燥为主。那如何解决多烘缸纸机干燥部过长的问题?请看新的干燥部设计方案——多列烘缸干燥部。 相似文献
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为了降低纸机干燥部热能消耗、提高水分蒸发效率,根据气压分布原理,通过各温湿参数内在关联机理和Matlab编程分析,从理论上系统地对干燥部温湿参数动态特征及热能节约原理进行了研究。研究表明,纸幅干燥曲线受烘缸蒸汽和进风状况共同影响,烘缸蒸汽消耗受进风状况影响;许多纸机干燥部虽运行正常,但是蒸汽消耗并非最低,可通过优化工艺参数,大大减少蒸汽用量;在保证产品质量的前提下,对热风交换系统零位进行优化调节与控制,可达到最佳节能效果。 相似文献
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有的工厂由于对于燥的强化措施不了解,出现了一些问题。例如,某中型厂为了提高纸机干燥速度,把原来的生蒸汽管道与第一段烘缸出来的二次蒸汽管道接通(即图中A、B两处用管道连起来),想借此提高二段烘缸内蒸汽温度,加快干燥速度.由于第一段烘缸进汽与出汽没有压差,对冷凝水排出不利,总的干燥效率反而可能下降.因此有必要对纸机干燥部 相似文献
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介绍了用于评估纸机烘干部蒸汽冷凝水系统的运行状态的常规检测方法。利用纸面温度测量、烘缸表面温度测量及袋区通风温度测量数据,依据纸页干燥的客观规律,对纸机干燥部蒸汽冷凝水系统运行状态进行分析,以发现蒸汽冷凝水系统中的问题。 相似文献
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为了进一步地降低纸机干燥部能耗、提高能源的利用效率,本课题提出了能耗协同控制的概念,即同时考虑烘缸内部蒸汽冷凝水热力系统的能量消耗与气罩通风热力系统的能量消耗,实现二次热能的循环综合利用。针对高强瓦楞纸机干燥部设计了一套基于西门子S7-300 PLC的能耗协同DCS控制系统,实现了干燥部上述系统的整合,不但能够降低纸机干燥部的能耗,也为干燥部全局优化方案的实现打下了基础。本控制系统已在多条高强瓦楞纸机生产线上得到了应用,收到了较好的节能效果。为了实现干燥部的全局优化,本课题搭建了基于数据驱动的控制策略优化控制框架,将工业现场的大量运行数据用于模型的修正并建立控制策略优化数据库,可以快速寻找与当前工艺条件最为匹配的优化控制策略,实现节能降耗。 相似文献
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This paper deals with the performance evaluation of a single layer drying process of green olives in a tray dryer using exergy analysis method. Green olive was used as the test material being dried. Drying process was realized at four different drying air temperatures (40, 50, 60 and 70 °C) and a constant relative humidity of 15%. The effects of temperatures and mass flow rates were investigated. Maximum exergy efficiency of the drying chamber was obtained at a temperature of 70 °C and a drying air mass flow rate of 0.015 kg/s with 0.0004 kg/s of olive. The exergy efficiency values were found to be in the range of 68.65%–91.79% from 40 °C to 70 °C with drying air mass flow rates of 0.01 kg/s–0.015 kg/s. 相似文献
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传统烘缸的结构会造成冷凝水无法排出,致使烘缸能耗增大。多通道烘缸以其新颖的结构设计使得这种现状有所改变。为更加清楚的了解多通道烘缸的改进特性,对此进行了相关研究。研究结果表明:蒸汽冷凝传热系数随着蒸汽质量流速的增大而增加,且冷凝传热系数的增加幅度也随质量流速的增加而变大。而随着蒸汽干度的增大,冷凝传热系数几乎呈线性增加。在蒸气冷凝流动过程中,沿其流动方向的冷凝传热系数也逐渐减小。 相似文献
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为解决纸机干燥部冷凝水系统末段存在冷凝水排出温度较高、吨纸蒸汽消耗大等问题,本课题提出应用升温型吸收式热泵(adsorption heat transformer, AHT)作为冷凝水系统余热回收设备。该设备可利用中间品位的余热与低温热源的热势差作为驱动,制取品位高于中间余热的热量,从而提高余热的利用率。本文在分析纸机干燥部蒸汽冷凝水系统热力系统现状及升温型吸收式热泵工作原理的基础上,给出了一种基于升温型吸收式热泵的多段供汽热力系统流程。通过LabVIEW仿真计算结果表明,应用升温型吸收式热泵的纸机干燥部蒸汽冷凝水系统具有更好的节能效果。 相似文献
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简要分析了我国烘筒烘干机节能技术开发的关键点,详述了烘筒烘干机蒸汽用量优化系统Atmoset SMT-12技术原理及在印染加工中的应用;实际应用结果表明,使用Atmoset SMT-12蒸汽优化系统蒸汽用量降低了20%~30%,减少了对环境空气的污染。 相似文献
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SHRINKAGE AND DENSITY VARIATIONS OF FRESH GREEN BEANS DURING DRYING IN AN INERT MEDIUM FLUIDIZED BED
ABSTRACT
In this article, the shrinkage and density variations of cylindrical fresh green beans were investigated in a fluidized bed dryer with energy carriers. A pilot‐scaled fluidized bed dryer was set up for performing the drying experiments. Glass bead particles were used as inert materials. The drying experiments were done with fresh green beans of several lengths using hot air as a heating agent with the temperature range of 30–50C, and the effects of various parameters, such as the presence of inert materials, temperature and sample length, were investigated. It was found that the shrinkage or volume changes, and radial and axial contractions of fresh green beans could be well correlated as linear functions of moisture content during drying. Calculated and experimental values were in good agreement with mean absolute errors (MAEs) of 3.56, 2.48 and 1.22 for volume changes, and axial and radial contractions, respectively. By considering that the change in the volume of the samples was equal to the volume of evaporated water, mathematical models were proposed for volume and density variations. Comparison of the predicted values for volume and density by the proposed model with experimental date showed that the uniform model of shrinkage could explain the shrinkage and density variations of fresh green beans with MAEs of 5.190 and 4.250 for volume and density variations, respectively. The shrinkage coefficients were evaluated by considering their measurement uncertainties.PRACTICAL APPLICATIONS
Any attempt to characterize drying behavior must inevitably address the physical parameters of the material such as shrinkage and density. The shrinkage phenomenon occurring during the drying process affects the physical properties of the solids, as well as the transport phenomena properties. The shrinkage of vegetables during drying is important not only from the viewpoint of material end use but also for simulation problems.17.
纸机的干燥部是造纸厂热能消耗的最主要部分,也是节能减排工作的重点,不同的干燥方式,能源的利用效率各不相同,能源成本也存在较大差异。本文介绍了蒸汽烘缸干燥及气罩系统以及常用于涂布纸的红外干燥、热风干燥的基本原理、能源利用效率及使用成本等,并定量计算进行了说明。从辐射的原理入手,详细解释电红外与燃气红外的异同,澄清人们对这两种红外干燥器能源利用效率的误解,文中的计算结果也为干燥系统的选用或优化提供了数据支持。 相似文献