效率和研磨介质填充水平

D. Longhurst, M. Wilczek
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Initial indications were that there was a very good possibility for increased efficiency if ball mills were run with drastically reduced filling levels. Unfortunately there was only a verbal presentation and discussion on the results; no written report was made and both men have since passed away. Mr. Longhurst was fortunate to have been associated with them and his initial introduction to grinding was through them, which is how he came to know of these tests. This presentation was given at a time when a 1000 horsepower ball mill was considered a “giant” and the goal was to get as much energy from the lowest mill volume requirement. For this reason, funded research for possible efficiency gains from low ball charge filling levels was not allowed by the corporation they worked for. To put maximum energy between the trunnion bearings in a short distance required a high filling level in the mill, making the actual grinding efficiency a secondary concern. These decisions made a great deal of sense then as slide shoe supported mills were not in use. As demand for mills with increased energy grew, the bending stresses on the mill shell between trunnion bearings also grew. Mill shell thicknesses increased and the head and discharge walls of trunnion supported mills became massive. The question as to whether or not energy was being effectively transmitted to the material being ground as the layers of balls increased in the grinding chamber remained unanswered. In other words, “Was there a change in efficiency relative to the filling degree of ball mills?” With the advent of shell supported mills and larger diameters, the bending stresses on mill shells were alleviated to a great degree. Slide shoe supported mills eased those concerns and made possible the lowering of “normal” filling levels of 40% to 45% to a new “normal” of 28% to 35%. Ten to fifteen years ago two events took place which seemed to support the results of the preliminary investigations of low level filling and efficiency. In the first case, one of the drives failed on a dual drive ball mill operating with a High Pressure Grinding Roll (HPGR)(1). Since delivery time for parts to repair the damaged drive was lengthy, a decision was made to reduce the charge in the ball mill from approximate 32% filling level to a point low enough to allow the mill to be operated with the single remaining drive. Surprisingly the result was a minimal loss in production, with a significant gain in efficiency. In the second case several years later, an opportunity arose which allowed commissioning of a new mill with a low ball charge level grinding granulated blast furnace slag to produce Grade 120 Slag cement (~5750 cm2/g). The results of this were briefly presented at the 2000 IEEE in a paper titled “SEPARATE SLAG GRINDING IN DIFFERENT MILLING SYSTEMS”(2). 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引用次数: 1

摘要

材料、仪器、监测技术、工艺知识的进步以及对效率和保护的不断增长的需求,为粉碎领域的研究开辟了道路,这些领域一直被忽视或一次又一次地被放弃。关于研磨的“艺术”,已有大量的论文和书籍。在过去的50年里,将特定矿物或材料减少到特定细度所需的比能量已经减少了一半,我们知道仍有可能进一步减少这一比能量。大约在60年前,Fred C. Bond, George Krouse和其他一些从事粉碎研究的人对实验室球磨机中研磨介质的低填充水平进行了一些初步研究。最初的迹象表明,如果球磨机在大幅降低填充水平的情况下运行,则极有可能提高效率。不幸的是,只有口头陈述和对结果的讨论;没有书面报告,两人都已去世。朗赫斯特先生很幸运与他们有联系,他最初接触研磨就是通过他们,这就是他如何知道这些测试的。这个演讲是在一个1000马力的球磨机被认为是一个“巨人”的时候进行的,目标是从最低的磨机体积要求中获得尽可能多的能量。出于这个原因,他们工作的公司不允许资助研究从低球电荷填充水平可能获得的效率提高。为了在短距离内将最大能量放在耳轴轴承之间,需要在磨机中提供高填充水平,从而使实际研磨效率成为次要问题。这些决定作出了很大的意义,然后滑鞋支持米尔斯没有在使用。随着对耗能增加的轧机的需求增加,轴承座之间轧机壳体的弯曲应力也增加了。轴承式磨壳厚度增大,磨头和出料壁变大。随着研磨室中球层的增加,能量是否被有效地传递给被研磨的材料,这个问题仍然没有答案。换句话说,“相对于球磨机的填充程度,效率是否有变化?”随着壳撑式轧机的出现和直径的增大,轧机壳体的弯曲应力得到了很大程度的缓解。滑动鞋支撑的工厂缓解了这些担忧,并使“正常”填充水平从40%到45%降至28%到35%的新“正常”填充水平成为可能。十到十五年前发生的两件事似乎支持了低水平填充和效率的初步调查结果。在第一种情况下,使用高压磨辊(HPGR)的双驱动球磨机的一个驱动器发生故障(1)。由于修复损坏驱动器的部件的交货时间很长,因此决定将球磨机中的装药量从大约32%的填充水平降低到足够低的水平,以允许球磨机使用单个剩余驱动器进行操作。令人惊讶的是,结果是生产损失最小,效率显著提高。在几年后的第二个案例中,出现了一个机会,允许使用一个新的磨矿机,该磨矿机采用低球量磨矿高炉矿渣,生产120级矿渣水泥(~5750 cm2/g)。这一结果在2000年IEEE上发表了一篇题为“不同磨矿系统中的分离渣磨”的论文(2)。从那时起,很少有人在商业规模上调查低填充水平的球磨机可能带来的好处。由于时间、费用和生产中可能的损失,直到最近才在商业磨机上进行这样的研究。考虑到能源成本的上升和市场的缓慢,随着新工厂的投产,降低比能导致能源成本降低的可能性为进一步研究这一现象打开了机会之窗。
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Efficiency and grinding media filling level
Advances in materials, instrumentation, monitoring techniques, process knowledge and an ever increasing demand for efficiency and conservation have opened the way to research in areas of comminution that have been overlooked or abandoned time and time again. There are a multitude of papers and books in existence concerning the “art” of grinding. Over the last 50 years, the specific energy required to reduce a given mineral or material to a specific fineness has been cut in half and we know there may still be possibilities to reduce this even further. About 60 years ago, Fred C. Bond, George Krouse, and a few others involved in comminution research conducted some preliminary studies on low filling level of grinding media in laboratory ball mills. Initial indications were that there was a very good possibility for increased efficiency if ball mills were run with drastically reduced filling levels. Unfortunately there was only a verbal presentation and discussion on the results; no written report was made and both men have since passed away. Mr. Longhurst was fortunate to have been associated with them and his initial introduction to grinding was through them, which is how he came to know of these tests. This presentation was given at a time when a 1000 horsepower ball mill was considered a “giant” and the goal was to get as much energy from the lowest mill volume requirement. For this reason, funded research for possible efficiency gains from low ball charge filling levels was not allowed by the corporation they worked for. To put maximum energy between the trunnion bearings in a short distance required a high filling level in the mill, making the actual grinding efficiency a secondary concern. These decisions made a great deal of sense then as slide shoe supported mills were not in use. As demand for mills with increased energy grew, the bending stresses on the mill shell between trunnion bearings also grew. Mill shell thicknesses increased and the head and discharge walls of trunnion supported mills became massive. The question as to whether or not energy was being effectively transmitted to the material being ground as the layers of balls increased in the grinding chamber remained unanswered. In other words, “Was there a change in efficiency relative to the filling degree of ball mills?” With the advent of shell supported mills and larger diameters, the bending stresses on mill shells were alleviated to a great degree. Slide shoe supported mills eased those concerns and made possible the lowering of “normal” filling levels of 40% to 45% to a new “normal” of 28% to 35%. Ten to fifteen years ago two events took place which seemed to support the results of the preliminary investigations of low level filling and efficiency. In the first case, one of the drives failed on a dual drive ball mill operating with a High Pressure Grinding Roll (HPGR)(1). Since delivery time for parts to repair the damaged drive was lengthy, a decision was made to reduce the charge in the ball mill from approximate 32% filling level to a point low enough to allow the mill to be operated with the single remaining drive. Surprisingly the result was a minimal loss in production, with a significant gain in efficiency. In the second case several years later, an opportunity arose which allowed commissioning of a new mill with a low ball charge level grinding granulated blast furnace slag to produce Grade 120 Slag cement (~5750 cm2/g). The results of this were briefly presented at the 2000 IEEE in a paper titled “SEPARATE SLAG GRINDING IN DIFFERENT MILLING SYSTEMS”(2). Since that time, little has been done to investigate the possible benefits of low filling level of ball mills on a commercial scale. The time, expense, and possible loss in production meant it was not feasible to perform such a study on a commercial mill until recently. With a new mill to be commissioned, considering rising energy costs, and a very slow market, the possibility of reduced specific energy resulting in lower energy costs opened a window of opportunity to investigate this phenomenon further.
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