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  • 게시판 | TBB Automation

    실제 작동 상태를 확인하려면 라이브 사이트로 이동하세요. 전체 게시물 카테고리 내 게시물 정렬: 최근 활동 전체 카테고리 팔로우 Create New Post Comments 조회 최근 활동 Item option menu what is secondary research Mollie Talbot · 일반 게시판 9 0 7월 01일 Forum - Frameless

  • 프로필 | TBB Automation

    페이지를 찾을 수 없음 존재하지 않는 페이지입니다. 메인 페이지에서 다른 페이지로 이동하세요. 메인 페이지로 이동

  • Textbook | TBB Automation

    Process Identification and PID Control Introduction Go Now Powerpoint Materials Go Now Corrections Go Now MATLAB m-files Go Now Virtual Process Package Go Now Solutions Go Now Introduction Process Identification and PID Control enables students and engineers to understand the essential concepts of feedback control, process identification, autotuning, and design of real feedback controllers, especially PID controllers. Sung, Lee, and Lee introduce the fundamentals of process control and dynamics, analysis tools (Bode plot, Nyquist plot), PID controllers and tuning, controller designs, along with the advanced control strategies which have been widely used in industry. Included are numerous numerical examples and MATLAB codes to aid the reader in solving real problems. Readers will be able to design their own controllers, implement them, and confirm performance in real-time using the real-time virtual processes. Combines the basics with recent research, helping the novice grasp advanced topics. Brings several industrially important topics together: Finishing topics with implementation codes Process identification and implementation PID controller tuning and implementation Enhanced control strategies and implementation Includes all source codes and real-time virtual processes for self-practice and modeling/controller design courses Contains problems at the end of every chapter Written by a team of recognized experts in the area Process Identification and PID Control is ideal for undergraduate and graduate students in process control, advanced process control, and process identification. Practicing control engineers and R&D personnel in refineries and chemical plants will find this book to be a key reference. Professionals in industry in particular will appreciate the techniques for developing process identification and control software, as well as implementing microprocessor controllers. Sites: http://as.wiley.com/WileyCDA/WileyTitle/productCd-0470824107.html http://www.amazon.com/exec/obidos/ASIN/0470824107/cern http://www.booktopia.com.au/process-identification-and-pid-control/prod9780470824108.html http://books.google.co.kr/books?id=HxyV2MDoY18C&dq=process+identification+and+pid+control&source=gbs_navlinks_s http://www.kyobobook.co.kr/product/detailViewEng.laf?ejkGb=ENG&mallGb=ENG&barcode=6100470824107 http://www.mightyape.co.nz/product/Process-Identification-and-PID-Control/3045548/ http://www.books.com.tw/exep/prod/booksfile.php?item=F011649749 MATLAB m-files MATLAB m-files for the book "Process Identification and PID Control" are attached. If you have any problems in downloading it, email to suwhansung@knu.ac.kr or contact TBB . Then, we will send you the m-files as soon as possible by email. Also, if you find any mistakes, please, let me know. Contact Us Powerpoint Materials The powerpoint files for the book are allowed to instructors only. Please, use the website at http://www.wiley.com/go/swsung to download the files. Or, we can send them directly through email if you want. Contact Us Virtual Process Package Virtual Process Package ver.1 is attached. Contact Us Corrections Page 15, "Equation (1.46) is valid for" should be replaced by "Equation (1.47) is valid for". Page 17, "Examples 1.27-1.29" should be replaced by "Examples 1.26-1.29". Page 25, "S(t-theta)" in the beginning of 1.3.6 section should be removed. Page 38, "du(t)/dt|_{t=-0.5} = 0" should be added to (1.203) in Example 1.59. Page 39, "d^3y(t)/dt" in problem 1.4 should be replaced by "d^3y(t)/dt^3". Page 41, "0.05(dy/dt)^2" in Problem 1.11(d) should be replaced by "0.05(dy/dt)". Page 44, "d^2u(t)/dt^2|_{t=-0.3} = 0" should be added to Problem 1.18(e). Page 52, "h_u(j)=h_u(j+1)" in Table 2.5 should be replaced by "h_u(j)=h_u(j+1);". Page 56, "%Eq.(2.49)" and "%Eq. (2.48)" in Table 2.8 should be replaced by "%Eq.(2.48)" and "%Eq. (2.49)". Page 70, "Euler = %7.5f" and "Trapezoidal = %7.5f" in Table 2.16 should be replaced by "Euler = %9.5f" and "Trapezoidal = %9.5f". Page 77, "(x1 -1)^3" of Problem 2.11 should be replaced by "(x(1) - 1)^4". Page 77, "(y_i - ... )^3" of Problem 2.12 should be replaced by "(y_i - ... )^2". Page 86, "at at t=0" in Example 3.3 shoul d be replaced by "at t=0" in Example 3.3. Page 89, "y(s)/u(s)" in Equation 3.28 should be replaced by "y(s)". Page 96, "G(iw)=|G(iw)|exp(iw)a" above (3.52) should be replaced by "G(iw)=|G(iw)|exp(iw)". Page 99, "w_L = delta_w;" in Table 3.1 should be replaced by "w_L = w-delta_w;" Page 100, "The scales of the x-axis and the y-axis of the phase angle plot" should be replaced by "The scales of the y-axis and the x-axis of the phase angle plot" Page 103, "g=exp(-0.2*s)/(s+2)^2;" in Table 3.2 should be replaced by "g=exp(-0.2*s)/(2*s+1);". Page 106, "-" sign should be placed at the position where the three streams (G_d(s)d_i(s),u(s),G_i(s)y(s)) in Figure P3.3 are summed for the operation of G_d(s)d_i(s)+u(s)-G_i(s)y(s). Page 123, all "pid_ex4" should be replaced by "pid_ex5". That is, m-files titled "pid_ex5.m" and "g_pid_ex5.m" should be used to simulate Table 4.5. Page 135, "y_p(k)" in Equation 4.65 should be replaced by "y_s(k)". Page 168, "ti=tid+0.05" in pid_itae2_ex1.m should be replaced by "ti=tid". Page 181, "(-0.3+1)" in Eq(5.31) should be replaced by "(-0.3s+1)." Page 189,"k=abs(g_mr_to_second(0));" in Table 5.16 should be replaced by "k=abs(g_mr_ex6(0));" But, the corresponding m-files are correct. Page 198, "4.0(1+0.3s)" in Problem 5.14 should be replaced by "1.5(1+0.3s)." Page 202, "or a single root is located on the zero" should be removed. "or there is a multiple root (such as a double root, triple root, etc) located on the zero" should be removed. Page 231, "y2(s)" should be moved to before Gp1(s) in Figure P7.1. That is, y2(s) = Gp2(s)u(s) + d(s). Page 242, 251, 348, 350, 354, 356, "ymin=0.0" and "ymax=0.0" in the m-files should be replaced by "ymin=10^10" and "ymax=-10^10" respectively. The corresponding m-files are corrected. You can download the updated m-files from this website. Although the corrections do not affect the simulation results in the book, the corrections are required if you apply them to more general cases. Page 253, "dt" in Equation 8.59 (first line) should be replaced by "dτ". Page 269, "φw" in the first line should be replaced by "φ_w". Page 315, "ys=0.0 for t<0" in problem 9.4 should be replaced by "ys=0.0 for t<5". Page 371, "y(t)=0.5" in Problem 12.5 should be replaced by "y_ref(t)=0.5". Page 371, "w(t)=u(t)+1.0" and "1+2z(t)" in Problem 12.7 should be replaced by "w(t)=u(t)+0.1" and "1+z(t)/2", respectively. Solutions The solutions of the problems in Chapter 1,2,3,4,5,7, and 12 are available for instructors. If you are an instructor and need the solutions, please, let us know(suwhansung@knu.ac.kr ).

  • Home | TBB Automation

    Your Best Process Automation Solutions Provider Our Mission Contributing to automation industries and academia through commercializing our research experiences and results. Introduction to TBB (pdf) Automation Software Read More System Integration Read More Process Automation/Control Consulting Read More Training Courses Read More

  • TBB Valve | TBB Automation

    TBB Valve High-performance Control Valve High-Performance Control Valve high resolution, low hysteresis, fast response, high accuracy Read More Wide Temperature Coverage -30°C~300°C Read More Easy & Simple Networking via Modbus RTU protocol Read More Low-Cost & Fast Delivery $500* within 2~4 weeks (*1/4" control valve) Read More High Performance Control Valve high resolution, low hysteresis, fast response, high accuracy High resolution under 0.01° Easy and Simple Networking With TBB valves, configuring valve networks becomes easy and straightforward. One PLC or one PC can communicate with multiple valves via the Modbus RTU protocol. Reading SV (current angle set value (degree) or current opening (%)) PV (current angle measured (degree) or current opening (%)) Valve address (integer) Writing SV (angle set value (degree) or opening (%)) Valve address (integer) Modbus Address List for TBB Valve Wide Temperature Coverage TBB valve covers a wide temperature range, usable in various environments from -30°C to 300°C. Low Cost & Fast Delivery Much lower cost than other control valves $500 for a 1/4"-tube valve Fast delivery within 2~4 weeks Contact Us

  • Operator Training Kit | TBB Automation

    Liquid Level Control System A training kit for practicing PID tuning and learning PROMONICON Components One(1) PC with PROMONICON, which includes PID controllers Real-time graph Process diagram (HMI) Data storage (in the form of *.csv) Remote experiment Four(4) tanks One(1) load sensor to measure the liquid level One(1) control valve to control the flowrate One(1) pump for pressurization One(1) data acquisition box or One(1) PLC for sensing and actuation Lecture note Contact Us

  • Consulting | TBB Automation

    Consulting on maximizing process productivity and minimizing costs Moving the process to more profitable operation regions Consulting on moving the process to more profitable operation regions through improving the automation system can achieve the followings: Improving production rate Reducing the costs of raw materials and utilities Stabilization Consulting on improving process control system to stabilize the process can achieve the followings: Reducing variance of process variables Improving product quality Better consistency in yield and production rate Analyze performances of control, sensors, and actuators Consulting on finding and fixing the problems of sensors and actuators. Valve problems such as air leak, low resolution, hysteresis, sticking and cost Sensor problems such as low resolution, bad circuits or wires Contact Us

  • Contact Us | TBB Automation

    Contact Us Room No. 311, Engineering Building No.9, 80, Daehak-ro, Buk-gu Daegu, Republic of Korea, 41566 tbb.automation@gmail.com suwhansung@knu.ac.kr Tel: +82 53-950-6838 Submit Thanks for submitting!

  • System Integration | TBB Automation

    System Integration: From Designing Automation Systems to Commissioning TBB can provide a system integration solution by combining the core technologies such as SCADA, instruments, networking, process simulation & design, robotics, and lab automation. System Integration Control Logic Design and System Identification Classical control theories (feedback control, feedforward control, auto-tuning, gain-scheduling, split-range control, etc.) Advanced control theories ( high-performance TBB0 control, iterative learning control (ILC), model predictive control (MPC), model-based PID control, etc.) System identification theories (time-series, state space, artificial intelligence, neural network, deep learning, etc.) Control performance monitoring (oscillation, resolution, hysteresis, offset, performance index, etc.) Instruments Sensors/actuators Micro-processors PLC Data acquisition modules Process Simulation & Design ASPEN PLUS ASPEN HYSYS PROII Customized simulators Fundamentals in chemical engineering (process control, thermodynamics, fluid dynamics, heat transfer, reaction engineering, separation process, etc.) Robotics Cartesian robots Collaborative robots Gantry SCADA HMI Operation/control logics Data manipulation Reporting Alarm Remote operation/control Networking Serial, OPC, TCP, UDP, ODBC Modbus, CAN, user-defined protocols Lab Automation Robots Analyzers automation Data analysis Image processing Contact Us

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