Strojniški vestnik Journal of Mechanical Engineering Strojniški vestnik - Journal of Mechanical Engineering (SV-JME) Aim and Scope The international journal publishes original and (mini)review articles covering the concepts of materials science, mechanics, kinematics, thermodynamics, energy and environment, mechatronics and robotics, fluid mechanics, tribology, cybernetics, industrial engineering and structural analysis. The journal follows new trends and progress proven practice in the mechanical engineering and also in the closely related sciences as are electrical, civil and process engineering, medicine, microbiology, ecology, agriculture, transport systems, aviation, and others, thus creating a unique forum for interdisciplinary or multidisciplinary dialogue. The international conferences selected papers are welcome for publishing as a special issue of SV-JME with invited co-editor(s). Editor in Chief Vincenc Butala University of Ljubljana, Faculty of Mechanical Engineering, Slovenia Technical Editor Pika Škraba University of Ljubljana, Faculty of Mechanical Engineering, Slovenia Founding Editor Bojan Kraut University of Ljubljana, Faculty of Mechanical Engineering, Slovenia Editorial Office University of Ljubljana, Faculty of Mechanical Engineering SV-JME, Aškerčeva 6, SI-1000 Ljubljana, Slovenia Phone: 386 (0)1 4771 137 Fax: 386 (0)1 2518 567 info@sv-jme.eu, http://www.sv-jme.eu Print: Grafex, d.o.o., printed in 380 copies Founders and Publishers University of Ljubljana, Faculty of Mechanical Engineering, Slovenia University of Maribor, Faculty of Mechanical Engineering, Slovenia Association of Mechanical Engineers of Slovenia Chamber of Commerce and Industry of Slovenia, Metal Processing Industry Association President of Publishing Council Branko Širok University of Ljubljana, Faculty of Mechanical Engineering, Slovenia Vice-President of Publishing Council Jože Balič University of Maribor, Faculty of Mechanical Engineering, Slovenia Cover: Corrosion is a factor significantly affecting the failure frequency of common rail systems. Destructive process can be concentrated locally to form a pit or crack, or it can extend across a wide area more or less uniformly corroding the surface. The consequences of its effect are accelerated wear of respective parts and assemblies, such as fuel injector nozzle tip and disc plate. Courtesy: The West Pomeranian University of Technology, The Department of Automotive Engineering, Poland ISSN 0039-2480 International Editorial Board Kamil Arslan, Karabuk University, Turkey Josep M. Bergada, Politechnical University of Catalonia, Spain Anton Bergant, Litostroj Power, Slovenia Miha Boltežar, UL, Faculty of Mechanical Engineering, Slovenia Franci Čuš, UM, Faculty of Mechanical Engineering, Slovenia Anselmo Eduardo Diniz, State University of Campinas, Brazil Igor Emri, UL, Faculty of Mechanical Engineering, Slovenia Imre Felde, Obuda University, Faculty of Informatics, Hungary Janez Grum, UL, Faculty of Mechanical Engineering, Slovenia Imre Horvath, Delft University of Technology, The Netherlands Aleš Hribernik, UM, Faculty of Mechanical Engineering, Slovenia Soichi Ibaraki, Kyoto University, Department of Micro Eng., Japan Julius Kaplunov, Brunel University, West London, UK Iyas Khader, Fraunhofer Institute for Mechanics of Materials, Germany Jernej Klemenc, UL, Faculty of Mechanical Engineering, Slovenia Milan Kljajin, J.J. Strossmayer University of Osijek, Croatia Janez Kušar, UL, Faculty of Mechanical Engineering, Slovenia Gorazd Lojen, UM, Faculty of Mechanical Engineering, Slovenia Thomas Lübben, University of Bremen, Germany Janez Možina, UL, Faculty of Mechanical Engineering, Slovenia George K. Nikas, KADMOS Engineering, UK José L. Ocana, Technical University of Madrid, Spain Miroslav Plančak, University of Novi Sad, Serbia Vladimir Popović, University of Belgrade, Faculty of Mech. Eng., Serbia Franci Pušavec, UL, Faculty of Mechanical Engineering, Slovenia Bernd Sauer, University of Kaiserlautern, Germany Rudolph J. Scavuzzo, University of Akron, USA Arkady Voloshin, Lehigh University, Bethlehem, USA General information Strojniški vestnik - Journal of Mechanical Engineering is published in 11 issues per year (July and August is a double issue). 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We would like to thank the reviewers who have taken part in the peerreview process. © 2015 Strojniški vestnik - Journal of Mechanical Engineering. All rights reserved. SV-JME is indexed / abstracted in: SCI-Expanded, Compendex, Inspec, ProQuest-CSA, SCOPUS, TEMA. The list of the remaining bases, in which SV-JME is indexed, is available on the website. The journal is subsidized by Slovenian Research Agency. Strojniški vestnik - Journal of Mechanical Engineering is available on http://www.sv-jme.eu, where you access also to papers' supplements, such as simulations, etc. Contents Strojniški vestnik - Journal of Mechanical Engineering volume 61, (2015), number 2 Ljubljana, February 2015 ISSN 0039-2480 Published monthly Papers Karol Franciszek Abramek, Tomasz Stoeck, Tomasz Osipowicz: Statistical Evaluation of the Corrosive Wear of Fuel Injector Elements Used in Common Rail Systems 91 Liao Yunfei, Zhou Yi, Liu Youhai, Zuo Dong, Tan Bo: Study of Stability of Precise Tiled-grating Device 99 Diego E. Lozano, Gabriela Martinez-Cazares, Rafael D. Mercado-Solis, Rafael Colas, George E. Totten: Estimation of Transient Temperature Distribution during Quenching, via a Parabolic Model 107 Yi Jiangang: Modelling and Analysis of Step Response Test for Hydraulic Automatic Gauge Control 115 Serkan Balli, Faruk Sen: Failure Prediction of Cross-Ply Laminated Double-Serial Mechanically Fastened Composites using Fuzzy Expert System 123 Xiaoming Huang, Jie Sun, Jianfeng Li: Effect of Initial Residual Stress and Machining-Induced Residual Stress on the Deformation of Aluminium Alloy Plate 131 Sebastian Baloš, Mladomir Milutinović, Michal Potran, Jelena Vuletić, Tatjana Puškar, Tomaž Pepelnjak: The Mechanical Properties of Moulded and Thermoformed Denture Resins 138 Strojniški vestnik - Journal of Mechanical Engineering 61(2015)2, 91-98 © 2015 Journal of Mechanical Engineering. All rights reserved. D0l:10.5545/sv-jme.2014.1687 Original Scientific Paper Statistical Evaluation of the Corrosive Wear of Fuel Injector Elements Used in Common Rail Systems Karol Franciszek Abramek - Tomasz Stoeck* - Tomasz Osipowicz The West Pomeranian University of Technology, The Department of Automotive Engineering, Poland This paper presents the causes and consequences of corrosion that has a destructive impact on the technical condition and operational reliability of Common Rail fuel injectors. The analysis included selected components indicating the elements and assemblies most frequently subject to destructive processes. Statistical evaluation of the corrosive wear of fuel injector elements was carried out based on experimental data obtained when verifying the fuel injector designs of different generations using the concept of corrosion density, related to our own classification of the degree of wear. The repair efficiency percentages were specified, taking into account specific operational mileages. Typical problems with the fuel injectors of leading manufacturers, with examples, are also shown. Keywords: common rail fuel injectors, component corrosion, statistical evaluation Highlights • Nozzle bodies and control valve assemblies proved to be most prone to corrosion. • The wear of electrical elements is least frequent. • An increase in the injection pressure leads to intensification of corrosive wear. • Repair is no longer effective with high operational mileages. • Availability of spare parts has a fundamental impact on fuel injector repair. 0 INTRODUCTION The process of wear can be defined as changes in the injection system as a result of use and leading to a gradual loss of functionality or permanent damage. Due to exceptionally difficult operating conditions, the elements of common rail systems being most prone to defects are fuel injectors [1]. Among other things, corrosion due to chemical or electrochemical mechanisms plays an important role in causing defects in fuel injection elements. Firstly, corrosion may affect sub-assemblies that have direct contact with the fuel and is found in the surface layers of friction pairs having different properties than the original material. Secondly, galvanic cells are formed which lead to reduction and oxidation reactions in the presence of electrolytes [2]. Accelerated wear may be defined as a situation in which the intensity of the formation of corrosion products (e.g. oxides, hydroxides) is higher than the surface destruction as a result of boundary friction. The corrosive effects of diesel oil depends largely on acidic oxygen complexes of natural origin or on the ageing processes being taking place in the oil itself, as well as on the content of sulphur and water compounds. Thus, the quality and type of fuel that feeds an engine substantially affects the intensity of the processes being discussed. Recently, fatty acid methyl esters (FAME) have been popularised as biodiesels, mainly for ecological reasons. Many researchers have shown, however, that fuels of this group are characterised by a high degree of oxidation [3], as well as a tendency to polymerisation [4] and deposit formation [5], and increased microbial degradation [6]. High hygroscopicity of FAMEs, affecting water absorption from the surroundings and increasing corrosion aggressiveness, is also very important. In some papers [7] and [8], it has been pointed out that corrosive action on metals is increased by the presence of alcohol, glycerol and free fatty acids. However, not all of these compounds are post-production residues of esterification. For example, it has been shown that dehydrated ethanol, applied in mixtures with FAME or diesel oil to improve starting properties, may have a corroding effect on the fuel pump and injector elements and, additionally, induce seal swelling and stiffening [9] and [10]. A separate issue is light heating oils, which are used illegally to fuel engines of commercial vehicles and to which red dye is added in order to identify the use of such oil. According to Kowalski [11], the properties of light heating oils do not fundamentally depart from those of diesel oils and their use should not cause major problems from the operational point of view. However, it is noteworthy that procedures for dye removal require the application of sulphuric acid, which has an exceptionally aggressive effect on metals. Attempts to neutralise this acid lead to the development of small grains initiating accelerated abrasive wear on the injection system. It has been *Corr. Author's Address: The West Pomeranian University of Technology, The Department of Automotive Engineering, Piastów 19 Ave., 70-310 Szczecin, Poland, tstoeck@wp.pl emphasised in another paper [12] that one of the elementary mistakes being made by the users of agricultural vehicles is the use of such heating oil, which leads to damages in the respective assemblies of force pumps and defects in fuel injector sprayers. Besides the quality and type of fuel, other factors having a significant impact on the intensity of corrosion occurrence are also noted in the reference literature. They include, among others, high temperature and pressure occurring in the combustion chamber [13], direct contact with fuel [14], ballistic phenomena [15], and turbulent fluid flow [16]. Researchers have also brought up the problems of accompanying processes, i.e. erosion [17] and cavitation [18]. Hence, a precision pair (needle and nozzle) affected by the phenomena mentioned above were examined. There are no data referring to other fuel injector elements and assemblies fulfilling executive and control functions. Our studies have shown that corrosion affects the parts of valve and armature assemblies almost equally. 1 EXPERIMENTAL METHODS The primary objective of this study was to statistically evaluate the corrosive wear of fuel injector elements of different types and manufacturers, taking into account the factors that have a negative effect on their operational reliability. In the analysis, the utilitarian nature of the repairs being conducted was also considered, and thus the possibility of eliminating the deficiencies being discussed, with a view to the degree of wear of respective parts and the possibility of their replacement. 1.1 Test Object The test object was common rail fuel injectors. A total of 3200 from a number leading manufacturers of fuel injection equipment such as Bosch, Delphi, Denso and Siemens were tested. Examination and verification of respective fuel injector components were conducted at the laboratories of VASCO Co. Ltd in Mierzyn, which co-operates with the Department of Automotive Engineering of the West Pomeranian University of Technology in Szczecin. The following equipment, among others, was used in this process: test benches (EPS 200 Bosch, Diesel Bench CRU 2 Zapp, Diesel Tech DS2 Zapp), a microscope with a camera to record digital images (FL150/70), ultrasonic cleaners (Elma Elmasonic S 10 H, Carbon Tech Ultrasonic Bath S15/C2), vices and fuel injector disassembly and assembly kits and a torque wrench set. Table 1. Graphical classification of corrosion and the criteria of adopted classification illustrated by examples (nozzle and valve seat) Level 0 Evaluation No corrosion Classification criteria No corrosion traces found Examples Level 1 Evaluation Low corrosion Classification criteria Corrosion covered up to 19% of the area of examined element Examples Level 2 Evaluation Moderate corrosion Classification criteria Corrosion covered 20 to 39% of the area of the examined element Examples Level 3 Evaluation High corrosion Classification criteria Corrosion covered over 40% of the area of the examined element (or was more localized nature but of high intensity) Examples 1.2 Scope and Criteria of Evaluation An experimental study was conducted according to our own methods, which included three implementation stages. In the first stage, fuel injectors were disassembled into components that were subject to detailed visual inspection and verification. Evaluation of the corrosion level was performed using visual methods as well as under a high magnification laboratory microscope. The next stage was initiated by cleaning in ultrasonic baths, excluding components sensitive to the effect of cleaning fluid, e.g. solenoid valves and injector bodies with embedded piezoelectric crystal stacks. The parts being qualified for replacement were also left out. After thorough drying and blowing off with compressed air, fuel injectors were assembled and then the test stage was conducted on test benches (last stage). Possible fuel delivery correction included only the designs for which unsatisfactory sampling results had been obtained. In order to conduct statistical analysis, the following visual levels of corrosion evaluation were established: 0 no corrosion, 1 low corrosion, 2 moderate corrosion, and 3 high corrosion. Examples of the graphical representation of adopted corrosion classification and its criteria are presented in Table 1. These fuel injector elements, which were eliminated due to pitting corrosion, most often of a local nature but of high intensity, are an exception. Although the size of the area affected by the changes was small, it was classified as level 3 (Fig. 1). a) b) Fig. 1. Examples of pitting corrosion; a) Bosch fuel injector nozzle tip, and b) Denso needle The results of the experiment were processed using the concept of corrosion density, the mathematical notation of which can be presented by the following equation [13]: IL D = — (1) where Dc is corrosion density, Li level of corrosion classification for the ith element and e is the number of elements. For example, when examining Bosch fuel injectors, corrosion density was determined as an algebraic sum of the verified corrosion levels which referred to the total number of examined elements e = 2368: D c ( Bosch, neddes) (1 + 0 + 3 +...) 2368 (2) 2 RESULTS AND DISCUSSION In Fig. 2 a histogram of the fuel injectors accepted for repair in VASCO over one year (11.2012-11.2013) is presented. 51-100 101-150 151-200 201-250 251-300 Operational mileages [thousand km] Fig. 2. Histogram of the fuel injectors accepted for repair in the test period Fuel injectors by Bosch constituted nearly 75%, which results from the dominance of this manufacturer in the segment of the automotive market under consideration. However, it is worth noting that 2/3 of them were from vehicle engines with mileage over 201,000 km. A similar correlation occurred only in Siemens products but these were solely piezoelectric fuel injectors, the maintenance of which was limited to cleaning and tests on test benches. Results for other fuel injector manufacturers constitute unimodal distributions, being characterised by moderate left- or e right-sided asymmetry. In this respect, fuel injectors of the Delphi design performed least favourably, showing increased failure frequency after mileage of 101,000 km. On the other hand, few problems are observed in the first and the last sections of the diagram. This is due to the fact that new vehicles are covered by the manufacturer's guarantee, while the questions of possible failures are usually examined at a service station. At the other end, few fuel injectors with high operational mileages were accepted because the efficiency of their repair was low. assembly, which is also exposed to corrosion (first of all in the head seat and flange), erosion and cavitation processes, occurs similarly [17]. The solenoid coil, having frequent contact with fuel compared to that of other manufacturers, should also be mentioned. The seating of the element through almost the whole length of the body causes problems with O-ring seals, which may occur even with low operational mileages. Losses in material and corrosion were observed in the fuel injectors of the Ford Transit, Focus and Mondeo vehicle models. 4 LjW^ k. ài -л л. Шч Ж. Type of element (assembly) Fig. 3. Comparison of corrosion density for selected elements (assemblies) of the examined fuel injectors Fuel injector nozzle bodies together with nuts and control valve assemblies proved to be the most prone to corrosion (Fig. 3). In the first case, a primary cause can be seen in the effect of high temperatures which induce accelerated degradation of the surface of metal, with an interaction of chemical and electrochemical reactions in the combustion chamber. However, it is worth noticing that corrosive processes affect the precision pair less, which has been confirmed by the results presented in paper [13]. For example, Delphi needles, being characterised by indents on the guide face made to preserve stable operation at higher pressures and under increased flow turbulence, performed most favourably in the given aspect. Corrosion mainly occurred in these depressions (Fig. 4a), while its traces were observed only in 42 elements from among 448 examined ones. Causes for increased failure frequency at relatively low mileages may be explained by the wear of fuel pumps, particularly of the drive areas of force assemblies, which generates metal fillings that get inside the fuel injector. The sharp edges of the needle indents induce jamming of hard impurities and accelerated seizing of the precision pair. Accelerated destruction of the control a) b) Fig. 4. Local corrosion of example parts of Delphi fuel injectors; a) needle and b) head The verification being carried out showed that the wear of armature assembly found solely in the fuel injector designs of two manufacturers proceeds similarly to that of the valve arrangements. Changes are usually seen on the surface of the disc (much less often on that of the insert) and elements co-operating with it (Fig. 5). With a similar construction and principle of operation, a comparable value for the parameter under discussion was obtained, i.e. D c(Bosch, armature assembly) = 0.22 and Dc(Denso, armature assembly) °.24. a) b) Fig. 5. Corrosion of Bosch fuel injector armature unit; a) disc plate and b) insert spring From among all elements being affected by corrosion, nearly 58% were classified at level 1. As a result, it was possible to remove corrosion traces after half-hour baths in ultrasonic cleaners. This is extremely important in the case of Denso products because availability of respective parts from this manufacturer, e.g. armature springs, locking rings and calibration washers, etc., is limited. Fig 0-50 51-100 101-150 151-200 201-250 251-300 Higher Operational mileages [thousand km] 6. Corrosion density according to operational mileages Interesting results were obtained when comparing the corrosion density to operational mileages (Fig. 6). Over almost the whole range, the values of the corrosion density parameter show an upward tendency, which results from an increasing number of degraded elements being included at higher and higher levels of corrosion. A crucial change can be seen in the last interval. The trend here is disturbed due to a rapid decrease in the number of fuel injectors being accepted for repair because they are effectively irrepairable. Nevertheless, the corrosion density there is definitely higher than with mileages of 0 to 150 thousand km. When analysing the presented data, one can conclude that the fuel injector designs using piezoelectric plate stacks by Siemens performed most favourably: wear traces on respective elements were observed less often and usually after a longer operation time. Unfortunately, both Siemans and Denso have a similar policy with respect to spare parts, i.e. there aren't any, which practically eliminates possibility of replacing these parts. The statistics for the elements of Bosch fuel injectors looks completely different. Within the mileage range of 201 to 300 thousand km, nearly 65% of all fuel injector designs of this manufacturer ware accepted for repair, obtaining as follows: Dc(Bosch, mileage: 201 to 150) = °.34 Dc(Bosch, mileage: 251 to 300) = °.47. These results are, at best, comparable with the others (except the Siemens products) but the market of available parts allows repairs over almost the full range, with the technology of this process being developed in detail and provided as needed. Relatively low values of corrosion density for the Delphi elements, particularly with moderate and high mileages, are also noteworthy. This means that increased failure frequency for these fuel injector designs depends largely on other factors. In this respect, improper co-operation of the control assembly (valve head and housing) and the precision pair (needle and nozzle) was the most frequently detected defect, resulting from accelerated abrasive wear of the co-operating surfaces. In recent years, a tendency has been observed to increase the injection pressure, which has a significant effect on the improvement of engine operational indicators and the reduction of emission of toxic exhaust gas components. Deterioration of operating conditions forced an increase in strength requirements which are being accomplished by changes in the design and materials. Results of our own study show that, despite these measures, the parts of injectors operating at higher pressures are more prone to corrosive wear. Due to the sample size and availability of respective fuel injector generations, an analysis was conducted solely for products made by Bosch (Fig. 7). In successive intervals, a growing number of elements in the highest level of the adopted classification can be observed. A similar situation was obtained with corrosion density, except at a pressure area of 200 MPa, in which solenoid fuel injectors of the CRI 2.5 (Common Rail Injector) type had been only examined. Nevertheless, the number of 3rd level parts was three times larger when compared with the initial area where such generations as CRI 1.0, CRI 2.0 and additionally CRIN 1, i.e. the fuel injector designs being applied in engines of commercial vehicles (German: Nutzfahrzeug), were examined. A similar correlation is being found for the elements operating at a pressure of 160 to 180 MPa. The obtained results point to the necessity of a much broader use of materials, of which mainly fuel injector nozzles have been made so far, i.e. stellite, carbide-steel cermets. These are characterised by large dimensional stability at high temperatures but also by abrasion and corrosion resistance and resistance to the ataggressive effect of fuels [19]. Table 2. Fuel Injector repair efficiency In the testing period a) Mileage ■ Number of repaired fuel injectors Bosch Denso Delphi Siemens 0-50 8 4 0 0 51-100 48 20 24 4 101-150 156 28 120 8 151-200 488 56 156 24 201-250 816 32 60 12 251-300 588 16 8 8 Higher 24 0 0 0 Summary ■ Total number of repaired fuel injectors 2128 156 368 56 Mileage Repair efficiency index at specific mileage [%] Bosch Denso Delphi Siemens 0-50 100 100 100 100 51-100 92 100 100 100 101-150 93 88 91 100 151-200 93 74 89 75 201-250 92 53 71 33 251-300 88 29 33 22 Higher 37 0 0 0 Summary Repair efficiency index for all manufacturer's designs [%] 90 61 82 44 [j j Operating p Fig. 7. Summary of results for Bosch fuel injectors working under different operating pressures; a) number of elements affected by corrosion and b) corrosion density The data presented in Table 2 suggest that repair is no longer effective at high operational mileages. In this respect, Bosch and Delphi fuel injectors, i.e. the designs of manufacturers offering the biggest product line of spare parts, performed most favourably. The fuel injectors being disqualified after main body defects (cracking, shape deformation, thread stripping) or defects in electrical elements (coil winding burnout, damages to piezoelectric crystal stack, breakage of terminal latches) had been found were an exception. The treatment was similar in the case of control solenoid valve corrosion. Attempts to remove corrosion traces using ultrasonic cleaners might result in undesirable softening of plastic housings and defects in insulation. Much lower repair efficiency indicators were obtained for fuel injectors from other manufacturers. In the case of Siemens, which specialises in piezoelectric fuel injectors, the maintenance essentially consisted of external and internal cleaning using only thermo-chemical methods and then to testing on test benches. Given the lack of availability of replacement parts by Siemans, the detection of more serious damages practically eliminated a given fuel injector. The repair of Denso products was possible over a slightly wider range. Some clients decided to use substitute parts that differ with respect to quality from the original elements, although they extend the service life of the fuel injectors. Replacement usually included the precision pair (deformation of needle taper, contact zone overheating, external and internal corrosion, guide face scratching or seizure) as well as control valve assembly (seat erosive changes, stem scratching, body surface and valve seating corrosion). 3 CONCLUSIONS The results of the above analysis show that corrosion is a factor significantly affecting the failure frequency of common rail systems. The consequences of its effect are accelerated wear of respective parts and assemblies, while products contaminate the interior of fuel injector and interfere with operating processes. The following conclusions have been drawn from this study: 1. The control valve and armature assemblies, which have direct contact with the fuel being supplied under high pressure, are equally affected by destructive processes of corrosion as nozzles. 2. The wear of electrical elements is least frequent but fuel injector is disqualified from further work (no cleaning or replacement possible). 3. As operational mileages continues to increase, corrosion density increases because corrosion traces are being observed in a larger number of parts, which are then classified as having higher and higher levels of wear. 4. An increase in the injection pressure leads to intensification of corrosive wear, despite design and material modifications in successive fuel injector generations. 5. Availability of spare parts has a fundamental impact on fuel injector repair efficiency because when they are missing (or limited) the elements or assemblies being affected by corrosion at higher levels cannot be replaced. 6. Limitation in the acceptance for repair of fuel injectors from engines with very high mileages results from their poor technical condition, most often precluding the recovery of nominal parameters. 4 NOMENCLATURE CRI common rail injector CRIN common rail injector (commercial vehicles) Dc corrosion density e number of elements FAME fatty acid methyl esters L level of corrosion classification for the ith element 5 REFERENCES [1] Knefel, T. (2012). Technical assessment of Common Rail injectors on the ground of overflow bench tests. Maintenance and Reliability, vol. 14, no. 1, p. 42-53. [2] Perez, N. (2004). Electrochemistry and Corrosion Science, 1st ed. Kluwer Academic Publishers, Boston, D0l:10.1007/ b118420. [3] Sharafutdinov, I., Stratiev, D., Shishkova, I., Dinkov, R., Batchvarov, A., Petkov, P., Rudnev, N. (2012). Cold flow properties and oxidation stability of blends of near zero sulfur diesel from Ural crude oil and FAME from different origin. Fuel, vol. 96, p. 556-567, D0I:10.1016/j.fuel.2011.12.062. [4] Shiwei, L., Lu, L., Shitao, Y., Congxia, X., Fusheng, L., Zhanqian, S. (2010). Polymerization of Fatty Acid Methyl Ester Using Acidic Ionic Liquid as Catalyst. Chinese Journal of Catalysis, vol. 31, no. 11-12, p. 1433-1438, DOI:10.1016/S1872-2067(10)60128-3. [5] Galle, J., Verhelst, S., Sierens, R., Goyos, L., Castaneda, R., Verhaege, M., Vervaeke, L., Bastiaen, M. (2012). Failure of fuel injectors in a medium speed diesel engine operating on bio-oil. Biomass and Bioenergy, vol. 40, p. 27-35, D0I:10.1016/j. biombioe.2012.01.041. [6] Schleicher, T., Werkmeister, R., Russ, W., Meyer-Pittroff, R. (2009). Microbiological stability of biodiesel - diesel -mixtures. Bioresource Technology, vol. 100, no. 2, p. 724-730, D0I:10.1016/j.biortech.2008.07.029. [7] Aquino, I.P., Hernandez, R.P.B., Chicoma, D.L., Pinto, H.P.F., Aoki, I.V. (2012). Influence of light, temperature and metallic ions on biodiesel degradation and corrosiveness to copper and brass. Fuel, vol. 102, p. 795-807, D0I:10.1016/j. fuel.2012.06.011. [8] Norouzi, S., Eslami, F., Wyszynski, M.L., Tsolakis, A. (2012). Corrosion effect of RME in blends with ULSD on aluminium and copper. Fuel Processing Technology, vol. 104, p. 204-210, D0I:10.1016/j.fuproc.2012.05.016. [9] Chauhan, B.S., Kumar, N., Pal, S.S., Jun, Y.D. (2011). Experimental studies on fumigation of ethanol in a small capacity diesel engine. Energy, vol. 36, no, 2, p. 1030-1038, D0I:10.1016/j.energy.2010.12.005. [10] Hansen, A.C., Zhang, Q., Lyne, P.W.L. (2005). Ethanol - diesel fuel blends - a review. Bioresource Technology, vol. 96, no. 2, p. 277-285, D0I:10.1016/j.biortech.2004.04.007. [11] Kowalski, K. (2006). Utilization of military vehicles under shortage of basic fuels. Maintenance and Reliability, vol. 4, p. 16-21. [12] Jósko, M., Kotodziejski, M. (2008). Selected exploitation problems of agricultural vehicles in the scope of their servicing. Journal of Research and Applications in Agricultural Engineering, vol. 53, no. 2, p. 5-7. [13] Taflan, R.A., Karamangil, M.I. (2012). Statistical corrosion evaluation of nozzles used in diesel CRI systems. Fuel, vol. 102, p. 41-48, D0I:10.1016/j.fuel.2012.06.037. [14] Günther, H. (2012). Common - Rail - Systeme in der Werkstattpraxis. Technik, Prüfung, Diagnose, 4th ed., Krafthand Verlag Walter Schultz GmbH, Bad Wörihofen. [15] Postrioti, L., Malaguti, S., Bosi, M., Buitoni, G., Piccinini, S., Bagli, G. (2014). Experimental and numerical characterization of a direct solenoid actuation injector for Diesel engine applications. Fuel, vol. 118, p. 316-328, D0l:10.1016/j. fuel.2013.11.001. [16] Boudy, F., Seers, P. (2009). Impact of physical properties of biodiesel on the injection process in a common-rail direct injection system. Energy Conversion and Management, vol. 50, no. 12, p. 2905-2912, D0I:10.1016/j.enconman.2009.07.005. [17] Olszowski, S. (2010). Examination of permeating oil causes in new generation diesel engines. Transcomp - XIV international conference, Computer systems aide science, industry and transport, vol. 6, p. 2581-2588. [18] Payri, F., Bermu'dez, V., Payri, R., Salvador, F.J. (2004). The influence of cavitation on the internal flow and the spray characteristics in diesel injection nozzles. Fuel, vol. 83, no. 4-5, p. 419-431, DOI:10.1016/j.fuel.2003.09.010. [19] Idzior, M. (2006). Tendencies of the construction changes in self-ignition engines injectors. Motrol - Motorization and Power Industry in Agriculture, vol. 8, p. 81-91. Strojniški vestnik - Journal of Mechanical Engineering 61(2015)2, 99-106 © 2015 Journal of Mechanical Engineering. All rights reserved. D0l:10.5545/sv-jme.2014.1658 Original Scientific Paper Study of Stability of Precise Tiled-grating Device Liao Yunfei - Zhou Yi* - Liu Youhai - Zuo Dong - Tan Bo College of Mechanical Engineering, Chongqing University, China To satisfy the high-stability requirement of a tiled grating, we have analyzed and optimized the stability of a newly designed precise tiled-grating device considering three aspects: structure design, transmission chain, and control algorithms. The main structure of the device is changed from a parallel-board structure to a new tetrahedral brace design, enhancing the overall vibration stability; during the analysis of the transmission chain, the adjustment accuracy and stability of the device were ensured by slowing the growth of the error transmission factor; and for the optimization analysis of the PID control algorithms, we adopted a latch compensation method to avoid the saturated loss and a four-point central difference method to avoid the disturbances, thus enhancing the stability control of the device. To test the stability of the device, an optical experiment with a reference spot was designed. The experimental results showed that over 380 s, the ambient excitation response was always within an acceptable range. The average deflections about the X axis and Y axis are 0.243 and 0.00146 /urad, respectively, which satisfy the stability requirement. Keywords: tiled-grating compressor, stability, dynamic response, tetrahedral, transmission chain, control algorithms Highlights • Showed a novel precise tiled-grating device. • Compared the vibration stability of two types of tiled-grating device. • Upgraded the transmission chain to decreased the error transmission factors. • Improved the incremental PID algorithm. 0 INTRODUCTION Chirped-pulse amplification (CPA) is an important technique for realizing amplification of ultra-short pulse lasers [1]. However, damage thresholds and the aperture of the compressor inside the CPA system limit the energy of the output laser pulse [2] and [3]. Currently, the grating with the best performance is the multilayer dielectric (MLD) diffraction grating, but it is very difficult to fabricate such gratings with sizes on the meter scale. Thus, most researchers around the world have adopted tiled gratings to obtain large gratings so as to enhance the energy of pulses output by lasers [4] and [5]. Because the quality of the laser beam depends upon stable tiled gratings as a key component [6], stability research on precise tiled gratings is important. In 2009, Zhong-xi et al. [7] devised a macro-micro dual-drive parallel mechanism with a few degrees of freedom for a tiled-grating device, and provided an error-correction method and control algorithms. In 2011, Zhou et al. [8] designed a tiled-grating structure with a large aperture and high precision in the form of a 2x2 array; the design is based on modularization and a frame-style structure to ensure the stability of the device. The experiment showed that the device can adjust rapidly in a timely manner and also that the stability time is greater than one hour. In 2011, Junwei et al. [9] suggested using a material with a high degree of damping to improve the connection status of the motion junction surface of the frame so as to lessen the dynamic response of the tiled brace and enhance the stability time. Here we describe and analyze a tiled-grating brace that is based on a newly designed tetrahedral structure and is designed to further enhance the stability of the tiled grating. To further improve the stability of the tiled grating, a novel tiling-grating device has been developed. A tetrahedral brace is used as the main body of the device to increase the natural mechanical frequency of the device. Additionally, a virtual tripod is built to fix the grating in place, and the transmission chain is improved to reduce the influence of transmission errors. In terms of the control techniques, because the four-point central difference method and latch compensation method have been used to improve the PID algorithm of the actuator, the short-term fluctuations in the control variable are smoothed out, and the influence of environmental disturbances is reduced. 1 TILED-GRATING SYSTEM This tiled grating consists of two sub-gratings, one of which is fixed and called the reference grating, and the other of which is an adjustable grating. The adjustable grating must take into account three degrees of freedom associated with the grating coordinates (x, *Corr. Author's Address: College of Mechanical Engineering, ChongQing University, No.174 Zheng Street Shapingba District, Chongqing 400044, China, cdzy@cqu.edu.cn 99 y, z): the tilt (6>y), tip (0x), and longitudinal piston (dz) (Fig. 1). Fig. 1. Tiled-grating frame structure The stabilization of a precise tiled grating relies on the structural stability of the vibration resistance of the device itself, the transmission precision and control stability of the device, and the ability of the control mechanism to compensate for environmental disturbances (Fig. 2). Therefore, we designed a tiled-grating device based on a tetrahedral structure; the tetrahedral structure enhanced the vibration stability of the device. We adopted an optimized transmission chain to increase the transmission precision and decrease the effect of errors; we also improved the control algorithm driving the actuator. As shown in Fig. 1, the device mainly consists of three parts: an adjusting component with three degrees of freedom, a grating brace, and a mount to hold the grating. Three piezoelectric actuators were used to adjust the three degrees of freedom. Overall stability Г 1 Г 1 r Random vibration Error transmission Control algorithm r 1 г л r Structural stability Transmission stability Stability of control Fig. 2. Schematic of the stability-control mechanism for the tiled-grating device 2 STABILITY ANALYSIS OF TILED-GRATING DEVICE 2.1 Vibration Stability of Tiled-Grating Device The mount that holds the whole precision tiled-grating device is composed of a baseboard and a tetrahedral brace. We modified the 2*2 parallel-board structure holding component of the tiled-grating brace to form a 2*1 brace. The finite-element random vibration analysis and Lanczos modal analysis of both of the tiled-grating frames are carried out using ANSYS software. In these analyses, the grating is defined to be formed from C9 glass; the other elements are defined to be formed from structural steel, and the bottom of the grating is assumed to be fixed. The analyses show that the vibrations of these points (marked by the points with teal labels in Fig. 3 along the top edge of each grating) have amplitudes that are as large as 5.2 and 9.1 цт, respectively. Both of these amplitudes are less than 12.9 ^m; therefore, the two devices meet the requirement given in [10]. Additionally, the tetrahedral mount has an important characteristic: the tetrahedral brace is a trussed structure; it helps in effectively decreasing the weight and enhancing the natural frequency of the structure. As shown in Table 1, the Phase 1 natural frequency of the tetrahedral brace was improved to 393.62 Hz; such a Phase 1 natural frequency can effectively avoid the risk of resonance. Fig. 3. Result of simulating the random vibration of two tiled-grating device designs; a) the parallel-board structure and b) the tetrahedral-brace structure Table 1. Natural frequency of two different tiled-grating frames ^\Modes 1 2 3 4 5 6 Parallel board 124.25 224.01 372.73 407.85 516.82 570.1 Tetrahedral brace 393.62 510.08 529.46 572.2 878.08 1013.4 2.2 Vibration Stability of Tiled-Grating Device In the device, the adjustment of the grating relies on the collective effect of the three drivers. Actuators 1 and 2 directly act on grating drivers 1 and 2, while actuator 3 transmits the driving force to grating driver 3 through the connection rod. When only actuator 3 is operating, the grating will rotate around the X axis. This movement is shown in Fig. 5 a; in this situation, there is only one degree of freedom. Slider A represents the piezoelectric actuator, Y represents the position of the piezoelectric actuator, the connection rod AB represents the rear connection rod, and the grating is along BC. Thus, the position of slider A is described by the equations: fy = r sina - L sin ß [L cos ß + r cosa = b (1) The partial derivatives of Eq. (1) are: BY _ cos(a + ß) 3Y_ _ dr sin ß dL sin ß dY — _- cot ß. (2) db Thus, we can see that the error transmission factors of each component, dY /dr, dY /dL, and dY /db, change with a, which is the angle between the grating surface and the horizontal plane. A plot of the values of the three error transmission factors against the angle a is shown in Fig. 4. 13л л 19n 32 2 32 a [rad] Fig. 4. Plot of the transmission error of each component against the angle a Fig. 5. Improvement of the mechanism for rotating about the X axis As shown in Fig. 4, within the considered value range, the three error transmission factors increase with a. For each error transmission factor, when it reaches a certain point, its value begins to increase rapidly. This means that the adjustment precision and stability of the grating are greatly affected. In order to decrease the impact of the growing error transmission factor, as shown in Fig. 5b, we moved the previous grating's adjustment point from the point B to the point B'; the grating itself remained in the same position, along the segment BC. Moving the grating's adjustment point decreases the angle a to a' = a-y, as shown in Fig. 5b. Decreasing this angle effectively shifts the operating point on each of the curves, as shown in Fig. 6. Therefore, the region of rapid increase is effectively avoided and the error transmission factors are lower in the new scheme. Fig. 6. The impact of the improvement about the error of each component against the angle a This result is equivalent to that obtained by adding a virtual tripod (ABCB') to support the grating and fixing this tripod to the original unmodified tiled device. However, the current tiled device has avoided the region with rapidly increasing error transmission factors, ensuring good adjustment precision and stability values. After the improvement, an experiment is carried out to test the vibration stability. The measuring points are the points labeled "Max" in Fig. 3, and the test time is 60 s. The experimental environment is different from the idealized simulation environment, so there are some acceptable differences between the two results. As shown in Fig. 7, the range of the vibration is narrower than before the improvement, which we regard as evidence that the vibration stability is improved under this new scheme. Statistical measures of the vibration in the two designs are given in Table 2. X io"3___^ 10 —Original , -e-Improved "50 10 20 30 40 50 60 Time [s] Fig. 7. Z-directional vibration comparison between the two tiled-grating devices Table 2. Statistical measures of the vibration of the two tiled-grating devices Max [mm] Average [mm] Variance Original 0.015 0.006 3.20x10-5 Improved 0.0057 0.002 6.80x10-6 2.3 Control Stability 2.3.1 Actuator Placement the Z axis by an amount Az. When actuator 3 stops and actuators 1 and 2 translate their respective points in opposite directions at the same time and with the same displacement, a rotation about the Y axis by an amount AOy is realized, and the central axis of this rotational adjustment is J. The spin degree of freedom around the X axis is realized when actuators 1 and 2 translate their respective points in the same direction at the same time with the same displacement while actuator 3 is translating in the opposite direction, and all three actuators impart the same displacement. A displacement can be added to this pure rotation by changing the amount of displacement associated with actuator 3. The central axis of this rotational adjustment is the horizontal central line I. Thus the adjustment of the three degrees of freedom of the grating is realized. Table 3. Relationship between the actions of the piezoelectric actuators and the DOF adjustments Actuator Adjusted direction +ox -Ox + Oy O +Z -Z 1 0 0 +Z -Z +Z -Z 2 0 0 -Z + Z +Z -Z 3 + Z -Z 0 0 +Z -Z As shown in Fig. 8, the component for adjusting the three degrees of freedom employed three actuators, numbered 1, 2, and 3, which respectively act on drivers 1, 2, and 3. Actuator 3 acts on the vertical central line of the rectangular grating's geometric center O. Actuators 1 and 2 act on the two sides of the vertical central line J. Fig. 8. Schematic showing the locations of the drivers The grating adjustment action is chosen based on Table 3. When actuators 1, 2, and 3 translate the grating in the same direction at the same time with the same displacement, the grating is translated along 2.3.2 Actuator Control Algorithm The scheme for controlling the actuator in this work is based on using 1) an incremental PID control algorithm, 2) a latch compensation method to avoid the saturated loss caused by the integrated saturation, and 3) the four-point central difference method to obtain differential parameters for anti-disturbance processing. As shown in Fig. 9, the theory of the latch compensation method is based on comparing the controlled quantity u with the controlled quantity of the actuator umax: if u < umax , then we use u; if u > umax , then we use umax . In addition, the difference Дм = u - umax is stored in a latch and added to the next u value. There is an obvious advantage to doing so, which is that although the last saturated loss is discarded, all the other controlled quantities are used, and the result is predictable and can be controlled within umax. In the digital PID algorithm, the disturbance corresponding to differential terms has a considerable effect on the control results. In PID control, it is generally necessary to adjust the differential terms although they cannot be eliminated easily. While the tiled-grating environment is standardized, there are many parameters that can change. The working environment of precise tiled gratings is subject to various disturbances [10] to [12]. All disturbances will impact the stability to a certain extent. In order to keep the grating stable over a long period of time and constrain most disturbances, we adopted the four-point central difference method [13] to modify the differential terms so as to control the disturbances. The basic theory is as shown in Fig. 10; the improved algorithm, when constructing a differential term, uses not only the current deviation but also the average deviations of the four-sample spot in the past and the present and then weights the sum to get a differential function similar to the form of Eq. (4), shown below. From signal processing theory, we know that by using the differential version of this method instead of the difference method, we can double the SNR (signal-to-noise ratio) [14]. Fig. 9. Diagram of the latch compensation method The general format of an incremental PID algorithm is: Aun = Kp (en - en-l) + Kien + Kd(en - 2en-l + en-2), (3) where Kp is the proportionality factor, K is the integration factor, Kd is the differential factor, and n indexes the samples. Using the four-point central difference method to process the differential factor, we get: ten = ^(e + 4-1 - 4-2 - en-3 ). (4) in Using Aen as a substitute for en- 2en-1 + en-2 Eq. (3), we can obtain the improved incremental PID algorithm: Aun = Kp (en — en—1 ) + Kien + 1 +—Kd (en + 2en—1 — 6en-2 + 2en-3 + en-4). 6 (5) We can see from the previous equation that the control increment in the incremental PID algorithm was improved using the four-point central difference method, because the short-term fluctuation is flattened to some extent. This mitigates the short-term fluctuation to a certain extent and reduces the impact caused by environmental disturbances. Furthermore, based on the step response shown in Fig. 11, the response speed of the improved PID algorithm is enhanced. Fig. 10. Four-point central difference method Fig. 11. Unit-step responses of the improved and classical incremental PID algorithms 3 EXPERIMENTAL VERIFICATION OF STABILITY OF TILED-GRATING DEVICE 3.1 Experimental Test To test and verify the stability of the prototype (Fig. 12) of the tiled-grating device, with existing resources, we designed a testing scheme, shown in Fig. 13. Fig. 12. Prototype of the tiled-grating device Fig. 13. Schematic of the stability-testing scheme There are four chief components: a 532 nm laser (which serves as the optical source), a 1:1 beam splitter, the tiled-grating device, and a target. The beam splitter and the tiled-grating device are parallel to each other, at a 45° angle with respect to the laser, 5 meters from the target. The laser beam emitted by the laser source is divided into two beams with equal energies, which we refer to as beams I and II. Beam I is projected onto the target after being reflected by the beam splitter; beam II is transmitted to the beam splitter and then projected onto the target after being reflected by a mirror on the tiled-grating device. Then, there are two spots on the target, as shown in Fig. 15. We use a camera to capture a photo of the spots on the target and obtain the relative position of the checked spot after image processing. In the process, the center of the spot is found to be the brightest position and it is used in calculations. In the tiled-grating device, the actuators are PSt 150/4/100 VS20 piezoelectric actuators, which include mechanical packaging, and the controller is a XE-500/501 PZT controller. Both the acutator and controller are manufactured by Harbin Core Tomorrow Science & Technology Co., Ltd. The resolution of the camera is 2 megapixels, and its frame rate is 5 FPS. In this stability experiment on the tiled-grating device, the general method for checking the far-field focal spot is not applied. If we used that method, whether the spot is focused would be checked qualitatively but not quantitatively; this is because the sharpness of the spots would change with changes to the displacement when the two spots are very close together (Fig. 14). When the computer program would analyze such images, the central point would be different in each image, and different measurement errors would be produced. It would therefore be difficult to obtain an accurate calculation. In our experiment, the spot's sharpness will remain unchanged, as shown in Fig. 15. Thus, all of the data produced by the image recognition program has the same measurement error in all of the images. The displacement between the two spots is defined as AS, which is used to characterize the vibration of the tiled grating device. The position of the reference spot in No.n image is defined as Srn and its measuring error is Ern. Correspondingly, the position of the checked spot in No. n image is defined as Scn and its measuring error is Ecn. Therefore, the distance between the two spots is Sn = (Srn + Ern) - (Scn + Ecn). The relative displacement between the twos spots is the distance difference between the two spots among neighboring images, that is, AS=Sn+1 - Sn. Because the measuring error remained unchanged, Esn = Es0 and Ecn = Ec0 always exist. Therefore, А5И = ^ - Sn = r (n+1) + Er (n+1) ) (Sc(n+1) + Ec(n+1) = [(S, - [(Srn + Ern ) - (Scn + Ecn )] = = ( Sr ( n+1) — Srn ) — (Sc ( n+1) — Scn ) )] - (2) The measuring error is removed. Here, the subscript 0 is the initial. aJ^^^^^^^M b) Fig. 14. Photographs of spots that are close together; a) focal spot and b) split spot [15] a) b) Fig. 15. Photographs of spots that are far apart; a) original configuration and b) after shifting The angular deflection response of the grating around the Y axis is: ey=arctan(ASX / L). (6) The angular deflection response of the grating around the X axis is: 0x=arctan(ASy / L). 3.2 Analysis of Experimental Results (7) In the process of the dynamic response testing, the total time over which the photographs of the spots are collected is 380 s, and the collection time interval is 4 s, resulting in a total of 96 photos. We use MATLAB to apply image processing to the photos collected by the camera and to find the relation between the time and the displacement response of the checked spot in the X and Y directions. Fig. 16. Displacement response curves of the checked spot in the X and Y directions From Fig. 16, we can see that the displacement response amplitude of the precision tiled-grating device in the Y direction is significantly greater than that in the X direction. With increasing time, the displacement response of the device shows no obvious increasing or decreasing trend, instead staying around the zero-displacement line. The statistics in Table 4 show that the variance yields of the displacement responses in the X and Y directions reached a level of 10-4, which shows that the amplitude of the average deviation of the displacement response is low. Therefore, it is practical to use the average value of the displacement response to represent the average value of the entire displacement response. Table 4. Statistical characteristics of the checked-spot displacement in the X and Ydirections Direction Max. amplitude Average value Variance yields X [mm] 9.84x10-2 -7.03x10-6 1.77x10-4 Y [mm] 1.51x10-1 -1.17x10-3 3.06x10-4 We substitute the average values of the displacement responses in the X and Y directions into the angle formulas, Eqs. (6) and (7), and find that the angular deflection response around the X axis of the precision tiled-grating device is: ex=arctan(1.17x10-3 / 5000) = 0.234 (rad. The corresponding value around the Y axis is: ey=arctan(7.30x10-6 / 5000) = 1.46x10-3 (irad. This result shows that the angular deflection responses around the X and Y axes are 0.243 (rad and 1.46xl0-3 (rad respectively, which satisfy the design requirement [10] of the SG-III system that the singleangle drift be less than 0.48 (rad. 4 CONCLUSION High stability is one of the critical requirements for a tiled grating. To determine how to realize a tiled grating with high stability, we analyzed the stabilities of newly designed tiled-grating devices. 1. The analysis results show that after the tiled-grating device is modified from the parallelboard structure to the tetrahedral structure, the natural frequency in Phase 1 is enhanced, and the maximum displacement of the device is transferred from the grating surface to the brace so that the vibration stability of the tiled grating is obviously improved. 2. Through investigation of the transmission errors of the device and the addition of a virtual tripod to avoid the region where the error transmission factor rapidly increases, we decreased the growth speed of the error transmission factor, and the impact on the control error was reduced. 3. To enhance the control stability of the device, a) we adopted a latch compensation method and the four-point central difference method to improve the PID control algorithm used by the device; b) we avoided the saturated loss, and the impact of environment disturbances was reduced; and c) the response speed was increased. 4. Our experiment showed that the stability of the sample device satisfied the target requirements of Ref. 10: over 380 s, the grating-angle drifts in the X and Y directions were 0.243 ^rad and 1.46*10-3 ^rad respectively. 5 ACKNOWLEDGEMENT This work was supported by the Research Fund for the Doctoral Program of Higher Education (20110191110006). 6 REFERENCES [1] Sharma, A., Kourakis, I. (2009). Laser pulse compression and amplification via Raman backscattering in plasma. Laser Part Beams, vol. 27, no. 04, p. 579-585, D0l:10.1017/ S0263034609990292. [2] Hornung, M., Bödefeld, R., Siebold, M., Kessler, A., Schnepp, M., Wachs, R., Sävert, A., Podleska, S., Keppler, S., Hein, J., Kaluza, M.C. (2010).Temporal pulse control of a multi-10 TW diode-pumped Yb: glass laser. Applied Physics B, vol. 101, no.1-2, p. 93-102, D0I:10.1007/s00340-010-3952-7. [3] Kessler, T.J., Bunkenburg, J., Huang, H., Kozlov, A., Meyerhofer, D.D. (2004). Demonstration of coherent addition of multiple gratings for high-energy ch i rped-p u lse-a m p l ifi ed lasers. Optics Letters, vol. 29, no. 6, p. 635-637, D0I:10.1364/ 0L.29.000635. [4] Blanchot, N., Bar, E., Behar, G., Bellet, C., Bigourd, D., Boubault, F., Chappuis, C., Coic, H., Damiens-Dupont, C., Flour, O., Hartmann, O., Hilsz, L., Hugonnot, E., Lavastre, E., Luce, J., Mazataud, E., Neauport, J., Noailles, S., Remy, B., Sautarel, F., Sautet, M., Rouyer, C. (2010). Experimental demonstration of a synthetic aperture compression scheme for multi-Petawatt high-energy lasers. Optics Express, vol. 18, no. 10, p. 1008810097, DOI:10.1364/OE.18.010088. [5] Guo-lin, Q., Jian-hong, W., Chao-ming, L. (2011). Laser pulse pattern influenced by mosaic grating gap. High Power Laser and Particle Beams, vol. 23, no. 12, p. 3177-3182, D0I:10.3788/HPLPB20112312.3177. (in Chinese) [6] Yan-lei, Z., Xiao-feng, W., Qi-hua, Z., Xiao, W., Yi, G., Zheng, H., Hong-jie, L., Chun-tong, L. (2006). Design of an arrayed grating compressor based on far-field. High Power Laser and Particle Beams, vol. 18, no. 10, p. 1619-1624. (in Chinese) [7] Zhong-xi, S., Qing-chun, Z., Qing-shun, B., Hong-ya, F. (2009). Design method of controlling device for tiling high pecision and large aperture grating. Optics and Precision Engineering, vol. 17, no. 1, p. 158-165. (in Chinese) [8] Zhou, Y., Shen, C., Zhang, J., Wang, X., Zhou, H. (2011). Structure design of high accuracy 2x2 array grating. High Power Laser and Particle Beams, vol. 23, no. 7, p. 1741-1745, D0I:10.3788/HPLPB20112307.1741. (in Chinese) [9] Jun-wei, Z., Xiao, W., Dong-hui, L., Hai, Z., Liang-ming, C., Xiao-min, Z., Feng, J. (2011). Dynamic Response Control and Analysis of Large Aperture Tiled Grating Mount. Acta Optica Sinica, vol. 31, no. 1, p. 158-162, D0I:10.3788/ aos201131.0112010. (in Chinese) [10] Mei-cong, W., Gang, C., Zhan, H., Xiao-juan, C., Wen-kai, W., Jun, W., Ming-zhi, Z. (2011). Stability design of switchyard in S G111 facility. Optics and Precision Engineering, vol. 19, no. 11, p. 2664-2670, D0I:10.3788/0PE.20111911.2664. (in Chinese) [11] Burkhart, S.C., Bliss, E., Di Nicola, P., Kalantar, D., Lowe-Webb, R., McCarville, T., Nelson, D., Salmon, T. (2011). National Ignition Facility system alignment. Applied Optics, vol. 50, no. 8, p. 1136-1157, D0I:10.1364/A0.50.001136. [12] Bernardin, J., Parietti, L., Martin, R. (1998). Thermal Issues Associated with the HVAC and Lighting Systems Influences on the Performance of the National Ignition Facility Beam Transport Tubes. Los Alamos National Lab., Los Alamos, D0I:10.2172/567499. [13] Jinbiao, W. (2004). Computer Control System. Tsinghua University Press, Beijing.(in Chinese) [14] Wen-bao, L., Li-xin, X., Xian-yi, Z. (1996). Research on Digital Control of Scanning Mirror Precise Servo System. Electrical Drive Automation, vol. 18, no. 04, p. 18-23. (in Chinese) [15] Jun-wei, Z., Wei, C., Na, X., Yi, Z., Hai, Z., Xiao, W., Feng, J., Xiao-min, Z.(2012). Design and demonstration of a tiled-grating frame. Optical Engineering, vol. 51, no. 1, p. 0130071-013007-5, D0I:10.1117/1.0E.51.1.013007. Strojniški vestnik - Journal of Mechanical Engineering 61(2015)2, 107-114 © 2015 Journal of Mechanical Engineering. All rights reserved. D0l:10.5545/sv-jme.2014.1997 Original Scientific Paper Estimation of Transient Temperature Distribution during Quenching, via a Parabolic Model Diego E. Lozano1* - Gabriela Martinez-Cazares2 - Rafael D. Mercado-Solis2 - Rafael Colas2 - George E. Totten3 i FRISA, México 2 Autonomous University of Nuevo Leon, México 3Portland State University, USA A material-independent model to estimate the transient temperature distribution in a test probe quenched by immersion is presented in this study. This model is based on the assumption that, under one-dimensional unsteady heat conduction, the radial temperature distribution at the end of an interval belongs to the equation of a parabola. The model was validated using AISI304 stainless steel test probes (Ф8*40 mm and Ф12*60 mm) quenched from 850 to 900 °C in water and in water-based NaNO2 solutions at 25 °C and in canola oil at 50 °C. Additionally, square test probes (20*20*100mm) were quenched from 550 °C in water. The test probes were equipped with embedded thermocouples for temperature-versus-time data logging at the core, one-quarter thickness and 1 mm below the surface. In each experiment, the data recordings from the core and near-surface thermocouples were employed for the temperature calculations while the data from the one-quarter thickness thermocouple were employed for model validity verifications. In all cases, the calculated temperature distributions showed good correlations with the experimentally obtained values. Based on the results of this work, it is concluded that this approach constitutes a simple, quick and efficient tool for estimating transient surface and radial temperature distributions and represents a useful resource for quenchant cooling rate calculations and heat transfer characterizations. Keywords: temperature distribution, quenching, parabola, heat transfer coefficient, cooling rate, cooling curve analysis Highlights • Parabolic model to calculate transient temperatures during the quenching. • Only the temperature histories of two points in the radial direction are needed. • The direct usage of simple algebraic equations minimizes calculation times with good accuracy. • The solutions are independent of material thermo-physical properties. • Heat transfer coefficient is directly solved via Fourier's law of heat conduction. • The model is an alternative to the Inverse Heat Conduction Problem (IHCP). 0 INTRODUCTION In heat treatment technology, quenchants with improved heat transfer properties and enhanced hardening capacities are under continuous development. In order to test such attributes, a common practice is to equip test probes with one or more thermocouples for temperature-versus-time data logging during a quenching cycle. By doing so, the speed at which heat is extracted from within the test probe (i.e. the cooling rate) can be calculated by means of cooling curve analyses, as per ISO 9950 [1], ASTM D6200 [2], ASTM D6482 [3] and ASTM D6549 [4], etc. From the metallurgical point of view, the knowledge of the cooling kinematics at the various heat transfer stages during the quenching of steel is an aspect of key practical importance. In this sense, a martensitic as-quenched microstructure would result from a sufficiently high cooling rate in order to avoid the pearlitic and bainitic transformations in the higher temperature range while cracking and distortion could be minimized by slower cooling kinematics in the martensitic transformation range at lower temperatures [5]. The cooling curves extracted from instrumented test probes may also be employed in the estimation of the surface temperature during quenching [6] and [7]. This may be further extended to calculate the heat transfer coefficient (HTC) and the heat flux densities (HFD) [8] to [11]. These two parameters adequately describe the overall heat transfer characteristics of a quenching system. The most popular technique for performing these calculations is the so-called inverse heat conduction problem (IHCP). In principle, the IHCP relies on the numerical solution of Fourier's well-known partial differential equation [12]. To solve the IHCP, the local temperature history (cooling curve) of one point inside the test probe should be known. Based on an initial "guess" of the HTC, an iterative calculation process is started to match the calculated temperature history with the measured one. In this way, the surface temperature may be estimated from the HTC values and from the thermo-physical properties of the test probe material (i.e. density, *Corr. Author's Address: FRISA S.A. de C.V., Santa Catarina, Nuevo Leon, Mexico, diego.lozano@frisa.com 107 thermal conductivity and specific heat capacity, etc.) within the quenching temperature range. Although the effectiveness of the IHCP has been extensively verified [13], the correct solution to the problem always remains largely dependent upon inputting the right thermo-physical properties, which are not easily measured. This is perhaps the main downside of the IHCP. In this paper, a relatively simple and straightforward approach for estimating transient temperature distributions and the surface temperature of a quenched part is presented. This model is based on the assumption that the temperature distribution inside the body follows a parabolic-type behaviour [14]. Thus, it may be regarded as an alternative to the IHCP, with the advantage that no thermo-physical properties are needed in the calculations, and that the direct usage of simple algebraic equations minimizes calculation times with acceptable accuracy. 1 DESCRIPTION OF THE PARABOLIC MODEL During the cooling of symmetric bodies under one-dimensional heat conduction, the assumption is made that the radial temperature distribution at the end of an interval belongs to an upside down parabola that is symmetric about the y axis defined as y=-ax2 + c and whose origin is at the center of the body at an arbitrary temperature [14]. Thus, by making the y axis the temperature and the x axis the radial distance from the center, the temperature Tc at the core of the bar (xc = 0) then corresponds to the vertex of the parabola, i.e. y = c = Tc (Fig. 1). Similarly, the temperature T2 at a radial distance from the centre x2 also belongs to the aforementioned parabola, and is, therefore, defined as: T2 =-0X2 + Tc . (1) Therefore, by solving Eq. (1) for a, we obtain: T - T (2) Based on the model assumptions, the temperature Trth at any given radial distance from the center xrth at the end of an interval shall also belong to the parabola, and is defined in the most general form as: Trth ~ aXrth By substituting Eq. (2) in (3), we obtain: Trth = (T - tc ) 2 + T. (3) (4) In summary, the implications of Eq. (4) are such that, during the cooling of a cylinder, the temperature of any point along the radial direction may be calculated if the temperatures of another two points along the same direction (T2 and Tc) are simultaneously known. Radial distance [x] Fig. 1. Parabolic temperature as a function of radial distance at the end of a quenching interval 2 EXPERIMENTAL VALIDATIONS In order to validate the parabolic model, a series of quenching experiments were performed using instrumented AISI 304 stainless steel test probes. In accordance with the minimum diameter-to-length ratio (1:4) practicable for one-dimensional heat conduction [15], two sizes of round cross-sectional test probes were fabricated: ф8*40 mm and ф 12*60 mm. Additionally, square cross-sectional test probes 20*20*100 mm were also quenched for comparison. Three ф1 mm blind holes were drilled in each test probe up to their mid-length at the core, one-quarter thickness and 1 mm below the quenched surface, as shown in Fig. 2. K-type thermocouples were tightly embedded in the holes for temperature-versus-time data logging during quenching. In order to prevent water from entering the thermocouple holes, zirconium oxide paint was used as a sealant. The thermocouples were differentially connected to a data acquisition card (NI USB-6211) using a 75 kW resistor between the negative of the thermocouple and the ground for a high electrical reference. Data was acquired at a rate of 100 samples per second and then smoothed through a cubic spline interpolation algorithm. This is an adequate method to a = 2 X 2 V X2 ) obtain an accurate global approximation over the time range [15]. The quenching experiments are summarized in Table 1. Quenchings were carried out inside a glass reservoir that contained 12 litres of quenchant. Tap water and sodium nitrite (NaNO2) aqueous solutions at concentrations of 1 and 9 % wt. were employed as quenchants. The initial temperature of the water and the water-based quenchants was 25 °C, while that of the oil was 50 °C. During the quenching experiments, a localized quenchant temperature increase (up to ~45 °C) was recorded with a thermocouple placed 50 mm away from the probe surface, but this increase was only limited to the regions adjacent to the test probe, while the overall temperature of the quenchant remained almost unchanged. After each experiment, the quenchant was stirred and left to cool down to 25 °C before the next experiment. The round test probes were quenched from temperatures of 850 and 900 °C, while the square test probes were quenched from 550 °C. Fig. 2. Drawings of the test probes and thermocouple positions; a) 012 mm round test probe; b) square test probe For each quenching experiment, the logged temperatures at the core (Tc) and at the near-surface (T„s) were input into the parabolic equation along with their radial distances. Therefore, the one-quarter thickness temperature (T'q) and the surface temperature (Ts) were calculated. Thus, for the new experimental notation, Eq. 4 may be suitably rewritten as: t \ =(Tm - Tc ) ( v Y (5) Ts = (Tns - Tc f У x„ + Tc . (6) The one-quarter thickness temperature readings were employed for model self-validations by comparing the experimentally obtained values (Tq) with the calculated ones (T'q) through Eq. (5). The temperature difference Tdif between T'q and Tq and their percent error were calculated for each quenching experiment as: rn _\rrf T Tdff - \Tq - Tq\ % error = —— X100. T (7) (8) Table 1. Summary of quenching experiments Experiment Type Size [mm] Temp. [°C] Quenchant 1 Round 08x40 850 Water 2 Round 08x40 850 9 % NaNO2 3 Round 08x40 900 Canola oil 4 Round 012x60 900 1 % NaNO2 5 Square 20x20x100 550 Water 3 RESULTS AND DISCUSSION The cooling curves obtained experimentally, and the calculated temperatures at the surface and one-quarter thickness are shown in the top charts of Figs. 3 to 7. The temperature difference and the percentage of error between the experimental and the calculated values at the one-quarter thickness are presented in the bottom part of the same figures. Fig. 3 shows the results of Experiment 1, in which, although the calculated curve does not generally overlap the experimentally measured one, they do follow the same trend. The maximum temperature difference occurred at the start of cooling where its influence upon the percentage of error is less due to the higher temperature values. The average error during the first 3 seconds was 4 %, while the average temperature difference was 17 °C. This is the interval where the curves overlapped less. Thereafter, the curves showed a good fit, and the highest temperature difference between the two remained within 6 °C and the error below 6 %>. Notice that the calculated surface temperature curve drops to 100 °C (boiling point of water) and, except for the small reheating obtained due to the internal heat source, the temperature remained near the v ns J K ns - T1 Core T2 2mm below surface \\ \ \ Surface (calculated) Temp. 2mm below surface (calculated) \\ \\ \\ \ \ \ \ \ > \ \ \ X \ \ \ • Error A AT p I— < -,---,-,-^-,-—To 0 1 2 3 4 5 6 Time [s] Fig. 3. Cooling curves of Experiment 1; a) temperature versus time, b) error % and temperature difference versus time 5 6 7 8 9 10 20 Time [s] Fig. 5. Cooling curves of Experiment 3; a) temperature versus time, b) error % and temperature difference versus time 2 3 4 5 Time [s] Fig. 4. Cooling curves of Experiment 2; a) temperature versus time, b) error % and temperature difference versus time 0 2 4 6 8 10 Time [s] Fig. 6. Cooling curves of Experiment 4; a) temperature versus time, b) error % and temperature difference versus time boiling point. This phenomenon is a self-regulating thermal process, in which the surface temperature does not cool below this point until sufficient heat has been extracted from the bulk of the probe [16]. Furthermore, since no agitation was used during quenching, localized heating of the quenchant up to its boiling point occurs. Thus, the surface becomes locally surrounded by the quenchant at the same temperature of the surface until the free convection of the fluid mixes it with the quenchant mass from more distant areas. In Experiment 2 (Fig. 4), a similar quenching was performed, except that sodium nitrite (NaNO2) was added in the water at 9 % wt concentration to promote a more severe cooling. Here, the film boiling (vapour) stage at the start of quenching is effectively suppressed. The boiling point of water is increased by salt additions and, thus, the surface temperature is expected to remain above 100 °C. From Fig. 4, it can be observed that, during the first three seconds, the error between the measured and the calculated temperatures reached a maximum of 4 %% and the maximum temperature difference was 16 °C. The average error and temperature difference for the first three seconds were 2.15 %% and 8 °C, respectively. At quenching intervals between 3 and 5 seconds, the average values were as low as 0.7 %> error and 0.7 °C temperature difference. The calculated surface temperature decreased to 133 °C due to the higher boiling temperature of the salt solution. The cooling curves of Experiment 3 corresponding to the 8 mm diameter bar quenched in canola oil are shown in Fig. 5. The heat extraction capacity of the vegetable oil is considerably lower than that of water and water-based salt solutions. Therefore, lower thermal gradients between the surface and the core of the test probe were measured. Since the temperature difference between the thermocouples was small, the error when calculating the temperature distribution was also small. The average error was only 1.8 %>, and the average temperature difference was 0.8 °C throughout the full quenching interval. For most of the time range, the error between the experimental and the calculated temperatures was less than 5 °C. Increasing the size of the sample did not produce any changes in the parabolic temperature distribution, as shown in the results of Experiment 4 (Fig. 6). Here, a 12 mm diameter bar was quenched in 1 %>wt NaNO2 aqueous solution. The calculated temperature using the parabola equation overlapped the experimental curve. The temperature difference always remained below 16 °C. On average, the error was 6.6 %% and the temperature difference 9 °C. In addition to the round bars, a bar of square cross-section was instrumented and quenched. The long square bar exhibits one-dimensional heat conduction at mid-thickness as would a slab. For Experiment 5 (Fig. 7), the square bar was heated to 550 °C followed by quenching in water at 25 °C. At the start of cooling, a stable vapour blanket formed around the probe. The calculated T'q temperature does not match the experimental data initially. This may be due to the inefficient heat transfer conditions established during this quenching stage and geometric effects. After the first 3 seconds, at which point the error reached 10 %% and the temperature difference reached a high value of 50 °C, the calculated data overlapped the experimental curve with a small difference of 4.5 °C and progressed to an almost exact fit thereafter. 10 15 Time [s] Fig. 7. Cooling curves of Experiment 5; a) temperature versus time, b) error % and temperature difference versus time 4 COOLING RATE CALCULATION EXAMPLE The rate at which cooling of the probes proceeds at any instant during quenching is determined by Newton's Law of Cooling. Here, a practical example of the use of cooling curve analyses for cooling rate calculations is presented for Experiments 2 and 3. The procedure involves the adjustment of the best-fit mathematical expression to each temperature-versus- time data set and its subsequant derivation; thus, dT/ dt is the cooling rate, which can be conveniently plotted against temperature and/or time. Fig. 8 shows the cooling rates obtained from Experiment 2 and the corresponding (calculated) surface temperature. It can be observed that the vapour phase is entirely suppressed; hence, very high cooling rates are achieved in the early stages of quenching at high temperatures. The addition of NaNO2 to the water result in high cooling rates reaching a maximum value of 1,300 °C/s as the surface temperature lowered to 700 °C. It is noteworthy that the maximum cooling rate is around 40 % higher at the surface that just 1 mm below it and 60 %% higher than the core. Cooling Fig. 8. Cooling rates of Experiment 2 100 150 Cooling rate [°C/s] Fig. 9. Cooling rates of Experiment 3 throughout the quenching cycle. Thus, the maximum cooling rate was 185 °C/s at a surface temperature of 700 °C. 5 HEAT TRANSFER COEFFICIENT CALCULATION EXAMPLE An example is presented for the calculation of the interfacial heat transfer coefficient from the surface temperature profile obtained through the parabolic model (appendix I). In references [15] and [17], Liščić and Filetin produced the experimental cooling data of the Liščić-Petrofer probe (ф50*200 mm) quenched in low viscosity accelerated quenching oil at 50 °C. These data have been reproduced in Fig. 10 and the surface temperature was calculated using the parabolic model. 10 100 1000 Time [s] Fig. 10. Experimental cooling data from references [15] and [17] and surface temperature calculation via the parabolic model 300 400 500 600 700 800 Surface temperature [°C] Fig. 11. Comparison of heat transfer coefficient calculation between the IHCP [15] and [17] and the parabolic model Similarly, the calculated cooling rates from Experiment 3 are shown in Fig. 9, where the film boiling phase was noticed at the start of quenching. After the vapour blanket was destabilized, the nucleate boiling phase is present until 350 °C was reached, followed by the convection stage. Due to the absence of large thermal gradients, the rate of cooling is nearly the same inside the test probe and on its surface Fig. 11 shows the comparison of the HTC results reported by Liščić and Filetin [15] and Liščić et al. [17] by solving the IHCP (solid line) and by the calculated surface temperature profile via the parabolic method in this study (dashed line). The maximum value of HTC calculated by the two methods matched 3,200 W/m2K. Moreover, a good agreement in the trend of the two curves was found. However, the surface temperature at which the maximum HTC occurs in each method differs by approximately 100 °C, i.e. the parabolic HTC curve is shifted towards the lower temperature range. In Liščić's method, the maximum value of HTC takes place when the maximum cooling rate of the surface occurs, whereas in the parabolic method, the maximum value of HTC takes place when the largest thermal gradient is set in the test probe. 6 CONCLUSIONS The parabolic model can correctly capture the radial temperature profile of test probes of various sizes and quenching media. For the analysis, only the temperature histories of two points in the radial direction are needed. Therefore, it provides the advantage that no thermo-physical properties are required, and the direct usage of simple algebraic equations minimizes calculation times with acceptable accuracy. Based on the results, it was concluded that this method is better suited for quenching in oil for which overly strong thermal gradients are not present, although entirely acceptable results were also obtained for water and aqueous solution quenchants. Once the surface temperature has been calculated, the procedure to determine the heat transfer coefficient and the heat flux density is highly simplified through the direct solution of the heat flux via Eq. (12) of Appendix. 7 ACKNOWLEDGEMENTS The authors wish to thank the following institutions for their support: Universidad Autonoma de Nuevo Leon, Facultad de Ingenieria Mecanica y Electrica and Consejo Nacional de Ciencia y Tecnologia (CONACYT-Mexico). 8 REFERENCES [1] ISO 9950:1995. Industrial Quenching Oils- Determination of Cooling Characteristics-Nickel-Alloy Probe Test Method. International Organization for Standardization, Geneve [2] AST M Standard D6200-01 (2012). Standard Test Method for Determination of Cooling Characteristics of Quench Oils by Cooling Curve Analysis. ASTM International, West Conshohocken. [3] ASTM Standard D6482-06 (2011). Standard Test Method for Determination of Cooling Characteristics of Aqueous Polymer Quenchants by Cooling Curve Analysis with Agitation (Tensi Method). ASTM International, West Conshohocken. [4] ASTM Standard D6549-06 (2011). Standard Test Method for Determination of Cooling Characteristics of Quenchants by Cooling Curve Analysis with Agitation (Drayton Unit). ASTM International, West Conshohocken. [5] Luty, W. (2010). Cooling media and their properties. Quenching Theory and Technology 2nd ed. Liscic, B., Tensi, H.M., Canale, L.C.F., Totten, G.E. (eds.). CRC Press, Boca Raton, D0l:10.1201/9781420009163-c12. [6] Meekisho, L., Hernandez-Morales, B., Tellez-Martinez, J.S., Chen, X. (2005). Computer-aided cooling curve analysis using WinProbe. International Journal of Materials and Product Technology, vol. 24, p. 155-169, D0I:10.1504/ IJMPT.2005.007946. [7] Hernandez-Morales, B., Lopez-Sosa, F., Cabrera-Herrera, L. (2012). A new methodology for estimating heat transfer boundary conditions during quenching of steel probes. Proceedings of 6th International Quenching and Control of Distortion Conference, p. 81-92. [8] Hasan, H.S. (2009). Evaluation of Heat Transfer Coefficients during Quenching of Steels. PhD. thesis, University of Cambridge, Cambridge. [9] Felde, I. (2012). Estimation of heat transfer coefficient obtained during immersion quenching. Proceedings of 6th International Quenching and Control of Distortion Conference, p. 447-456 [10] Lubben, T., Rath, J., Krause, F., Hoffman, F., Fritsching, U., Zoch, H. (2012). Determination of heat transfer coefficient during high-speed water quenching. International Journal of Microstructure and Materials Properties, vol. 7, no. 2-3, p. 106-124, DOI:10.1504/IJMMP.2012.047494. [11] Felde, I. (2012). Determination of thermal boundary conditions during immersion quenching by optimization algorithms. Materials Performance and Characterization, vol. 1, no. 1, p. 1-11, D0I:10.1520/MPC104417. [12] Beck, J.V. (1970). Nonlinear estimation applied to the nonlinear inverse heat conduction problem. International Journal of Heat and Mass Transfer, vol. 13, p. 703-716, D0I:10.1016/0017-9310(70)90044-X. [13] Landek, D., Župan, J., Filetin, T. (2014). A prediction of quenching parameters using inverse analysis. Materials Performance and Characterization, vol. 3, no. 2, p. 229-241, D0I:10.1520/MPC20130109. [14] Harding, R.A. (1976). Temperature and Structural Changes during Hot Rolling. PhD thesis, University of Sheffield, Sheffield. [15] Liščić, B., Filetin, T. (2012). Measurement of quenching intensity, calculation of heat transfer coefficient and global database of liquid quenchants. Materials Engineering -Materialové inžinierstvo, vol. 19, no. 2, p. 52-63. [16] Kobasko, N.I. (2012). Effect of accuracy of temperature measurements on determination of heat transfer coefficient during quenching in liquid media. Journal of the ASTM International, vol. 9, no. 2, p. 126-141 D0I:10.1520/ JAI104173. [17] Liščić, B., Filetin, T., Landek, D., Župan, J. (2014). Current investigations at quenching research centre. Materials Performance and Characterization, vol. 3, no.2, p. 3-18, D0I:10.1520/MPC20130102. [18] Holman, J.P., (1997). Heat Transfer. 8th ed. McGraw-Hill, New York. 9 APPENDIX: HEAT TRANSFER COEFFICIENT CALCULATION If a semi-infinite hot cylinder is suddenly quenched, then the heat flux will occur in one dimension according to Fourier's law of heat conduction. The energy balance for convection is therefore expressed as [18]: !AdT -kA— dx surface hA (surface Tos) (9) The finite-different numerical solution of unsteady-state conduction with convection boundary condition: -k £ (+i - Tm ) = hAy (Tm+1 - Tj), (10) T = m+1 Tm + (hAx/k )) 1 + (hAx/k ) ' where Tm+1 is the surface temperature, Tm is the near-surface temperature, Ax is the distance between the two positions, To> is the quenchant temperature, h is the heat transfer coefficient and к is the thermal conductivity. If the surface and near-surface temperatures are known, then the heat transfer coefficient may be calculated as: h = - k_ (Tm+l - Tm ) Ax (Tm+l - Tj (12) Strojniški vestnik - Journal of Mechanical Engineering 61(2015)2, 115-122 © 2015 Journal of Mechanical Engineering. All rights reserved. D0l:10.5545/sv-jme.2014.2046 Original Scientific Paper Modelling and Analysis of Step Response Test for Hydraulic Automatic Gauge Control Yi Jiangang* 1 Jianghan University, Hubei Key Laboratory of Industrial Fume & Dust Pollution Control, China The step response for hydraulic automatic gauge control (HAGC) determines the steel rolling speed and the steel sheet thickness in the process of rolling production. In this paper, the step response test process of HAGC was analysed, and a test approach was proposed for it. Based on that, the transfer function model of the step response test was established and simulated by using Matlab. In order to reduce the settling time and the overshoot, an adaptive proportional-integral-derivative (APID) link was presented in order to compensate for the input signal by using back propagation neural networks (BPNN). The experimental results show that the improved step response test model reaches the process requirements of HAGC, eliminates the jitter of the HAGC system at the start-up phase, and has better stability as well as faster response for steel sheet rolling. Keywords: step response, hydraulic automatic gauge control, proportional-integral-derived controller, artificial neural networks Highlights • Proposed the step response test model of HAGC system. • The working parameters study of the model. • Presented an APID link for signal compensation. • Representation of the stability and the flexibility on step response of the HAGC system. 0 INTRODUCTION Sheet gauge is one of the main quality indicators for steel sheet in the process of rolling production. To improve the control precision of sheet gauge, hydraulic automatic gauge control (HAGC) is currently widely used. In the process of HAGC, the step response plays the most important role, because it determines the steel rolling speed and the steel sheet thickness, and accordingly influences steel sheet surface quality. The step response test is a time-domain test method for system dynamic characteristics. It is used to describe the dynamic response process of the control system when the input is a step signal. To achieve uniform thickness of a steel sheet, the step response parameters of the HAGC should be adjusted according to the real-time thickness of steel sheet. However, during the step response process of HAGC, the step response parameters are influenced by the interactions of hydraulic cylinders, servo valves, and various sensors of the system, and the working time is extremely short (no more than 1 second). Consequently, it is of vital importance to model, test, and analyse the step response of HAGC. In terms of HAGC system design, Wang et al. and Taleb et al. developed a real-time simulator for a hot-rolling mill based on a digital signal processor, which can be used for controlling the hydraulic cylinder in an HAGC system [1] and [2]. Gao et al. proposed a simulated model of 1100 mm rolling mill HAGC system by using position-pressure compound control method [3]. T.S. Tsay presented a command tracking error square control scheme, and designed feedback control systems [4]. To achieve good control effect, many researchers studied the control algorithm of HAGC. Ang et al. and Mitsantisuk et al. researched the general design method of control system with proportional-integral-derived controller (PID) [5] and [6]. Zhang et al., Dou et al. and Chang et al. analysed the PID parameters setting problem [7] to [9]. Their research proved that the PID controller with proper parameters was efficient, but the setting of the PID parameters is the main problem. To achieve the desired strip thickness of the HAGC system, Khosraviet al. and Song et al. proposed a novel fuzzy adaptive PID controller [10] and [11]. The simulation results showed that it was better than traditional PID controller, but sensitive to parameter variations. Wan et al. and Kasprzyczak et al. analysed the main parameters of the hydraulic system and discussed their effects on system stability [12] to [13]. To solve the problem of multivariable parameters adjustment of the PID controller, several authors proposed some intelligent algorithms, such as evolutionary algorithms, particle swarm optimization (PSO), artificial neural networks (ANN) and generalized predictive control method [14] to [18]. The results indicated the intelligent algorithms improved the adaptability of the PID controller. However, the dynamic response process of the controller under step- *Corr. Author's Address: Hubei Key Laboratory of Industrial Fume & Dust Pollution Control, Jianghan University, Wuhan, 430056, China, Yjg_wh@yeah.net 115 input was not discussed. In the literature, the research put emphasis on the design, analysis and control of HAGC, and few papers studied the step response test of HAGC. In this paper, the step response test of HAGC is analysed, a test approach is proposed, and a transfer function model of the step response test is established and simulated by using Matlab software. In order to reduce the settling time and the overshoot, an adaptive proportional-integral-derivative (APID) link is presented to compensate for input signal by using back propagation neural networks (BPNN). The experimental results show that the improved step response test model reaches the process requirements of HAGC, eliminates the jitter of the HAGC system at the start-up phase, and has better stability as well as a faster response for steel sheet rolling. The structure of this paper is organized as follows. Section 1 introduces the parameters and the approach of the step response test of HAGC. Section 2 establishes the step response test model with transfer function. Section 3 simulates the proposed model by using Matlab, and presents the improved model of the step response test by adding an APID link based on BPNN. Section 4 contains the experiments and the analysis of the improved model. Section 5 is devoted to the conclusions. 1 THE STEP RESPONSE TEST OF HAGC 1.1 The Parameters of the Step Response Test In Fig. 1, the X coordinate value of the response signal curve represents the step response time, and the y coordinate value represents the displacement of the piston rod in the HAGC system. Next, the parameters of the step response test include the rise time tr, the maximum overshoot Mp, and the settling time ts. The rise time tr is the time at which the response signal reaches the first steady-state output, as described in Eq. (1): К ^0.9 10.1, (1) where t09 is the time at which the response signal is 90% of the first steady-state output, and t01 is the time at which the response signal is 10% of the first steady-state output. The difference between the response signal and steady-state output functions as the numerator, and the steady-state output as the denominator, the overshoot as the ratio of them. Next, the maximum overshoot Mp can be calculated by Eq. (2): MP = ■ (tp )- ■ (да) x100%, (2) where xo(t) is the displacement of the piston rod at the time t, and tp is the time at which the response signal reaches the peak. In the step response process, the settling time ts is also called the transition time, which represents the time at which the HAGC system reaches the steady-state. It is defined as the time at which the value of xo(t) satisfies Eq. (3): |x0(t)-x»| < 0.05x». (3) Fig. 1. The parameters of the step response test In the parameters of the step response, the settling time ts reflects the flexibility of the HAGC system, and the maximum overshoot Mp reflects the stability of HAGC system. In an HAGC system, it is always considered that the shorter of ts and Mp, the better of the control effect. 1.2 The Approach of the Step Response Test The main components in the step response process of HAGC are the servo valve, mill cylinder, current sensors, and displacement sensors. In order to simplify the test process, the influence of the hydraulic pipe and hydraulic power components is neglected. Next the approach of the step response test is shown in Fig. 2, and the main test steps are as follows: Step 1: The displacement of step signal is given to the computer test software. It is converted to a voltage signal by the data acquisition card and is sent to the current sensor (6). Step 2: The output signal of the data acquisition card is converted to current by the current sensor (6), and then is sent to the servo valve (5) to control the output flow in valve port A. Step 3: According to the output flow in the valve port A, the piston rod (3) of mill cylinder 2 moves up-down to control the rolling thickness of steel sheet. Step 4: The real-time displacement of the rolling thickness is measured by the displacement sensor (4), and then is converted to digital signal by the data acquisition card. Step 5: The acquired digital signal is sent to the computer test software, which will be compared with the input displacement in Step 1 to determine the next input value. 2 MODELLING OF THE STEP RESPONSE TEST 2.1 The Parameters of the Step Response Test According to Fig. 2, the step response test scheme is established, as shown in Fig. 3. The input signal Uv is the step signal of the expected displacement. The output signal Yp is the real-time displacement of the mill cylinder, which is converted to the voltage signal Up by the displacement sensor and fed back to the input port of the servo valve. The difference between Uv and Up, Ue, is converted to the current signal by the current sensor and is used to drive the servo valve. The piston rod action of the mill cylinder is controlled by the output flow of the servo valve. If the PID link is neglected and the input signals are sent to drive the servo valve directly, the transfer function of the servo valve is: (s ) = - к 2„ (4) s +1 where Ksv is the output flow gain of the servo valve, ajsv is the natural frequency of the servo valve, and 4v is the damping radio of the servo valve. The transfer function of the mill cylinder is: A G2( s) = - KK +1 2%h у (5) s +1 where mr is the transition frequency of the inertia, and mh and 4 are the natural frequency and the damping radio of the mill cylinder. Kce is the overall flow-pressure coefficient, K is the load stiffness, and Ac is the effective area of the piston rod of the mill cylinder. The transfer function of the current sensor is: 2 S Fig. 2. The step response test of HAGC; 1-Steel sheet, 2-Mill cylinder, 3-Piston rod, 4-Displacement sensor, 5-Servo valve, 6-Current sensor Modelling and Analysis of Step Response Test for Hydraulic Automatic Gauge Control 117 G3 (s ) = K, (6) where K is the gain of current. The transfer function of the displacement sensor H (s ) = Ks, (7) where Ks is the feedback coefficient of displacement. 2.2 Adding PID Link To reduce the settling time and the maximum overshoot of HAGC, some researchers proposed compensating for the input signal by using some algorithms. The signal compensation is implemented by adding a new link to improve the system performance. Because the PID algorithm is flexible, and its parameters can be easily adjusted, it is widely used in control systems. Therefore, based on the step response test scheme, a PID link is added in the step response test scheme between the input signal Ue and the current sensor, as shown in Fig. 3. The PID algorithm includes a proportional part, an integral part, and a differential part. Consequently, three coefficients, Kp, T and Td, are used in PID controller for the system control, where Kp is the proportional coefficient, Ti is the integral coefficient, and Td is the derivative coefficient. Therefore, the conventional PID algorithm can be described as: G4 (s ) = UL = Kp +-1 4 v > TT p т„ U. Ts + Ts. (8) In terms of Fig. 3 and Eqs. (4) to (8), the overall transfer function model of the step response test with conventional PID algorithm can be described as Eq. (9): G(s) H (s) = - K KK + ^s +1 +1 s — + a a 22ks+il (9) ■ KK ■ ( k p + Ts + Tds). 3 SIMULATION AND IMPROVEMENT OF THE STEP RESPONSE TEST 3.1 Simulation of the Step Response Test To analyse the control effect with and without a PID link in the step response test, the working parameters are loaded to the established transfer function model in the HAGC system, and the step response test is simulated by using the Simulink toolbox in Matlab software. The simulated model with the working parameters is shown in Fig. 4. In the simulated model, a step signal of 1 mm displacement is loaded at the input point, and the output result is shown as the blue dot curve in Fig. 5. In Fig. 5, it can be observed that ts = 140 ms, Mp = 25 %. However, in the HAGC production process, it is necessary that ts < 100 ms and Mp < 10 % for steel sheet rolling. Therefore, the settling time and the maximum overshoot are beyond the range of the HAGC requirements, which means the step response test without a PID link cannot be used to drive the HAGC system directly. Step signal PID Current sensor Servo valve Mill cylinder U„ Displacement sensor Fig. 3. The step response test scheme Fig. 4. The simulated model with working parameters A 2 s 2 Fig. 5. The simulated results of the step response test By adding the PID link in the established model in Fig. 4, the step response test is simulated with a conventional PID algorithm, and the output result is shown as a green solid curve in Fig. 5. It is found when Kp = 10, T = 50, and Td = 0, the settling time ts = 80 ms, and the maximum overshoot Mp = 9 %, which meet the process requirements of the HAGC. Moreover, testing shows that increasing Kp and Td, and decreasing T can further reduce the values of ts and Mp. However, at the same time, it leads to large jitters in the rise time of the step response test, which impairs the stability of the HAGC system. 3.2 Improvement of the Step Response Test The simulation results of the model with a PID link indicate that the contradiction between the stability and flexibility of the HAGC system cannot be solved by the conventional PID algorithm. This is because the PID parameters of the conventional PID algorithm are constant during the process of the step response test, which cannot be adjusted according to the input and output signals adaptively. In the actual production of steel sheet, because of the interactions of the servo valve, mill cylinder, and sensors in the HAGC system, the step response is a nonlinear time-varying process. K€ IL—