| 학회 | 한국화학공학회 |
| 학술대회 | 2011년 가을 (10/26 ~ 10/28, 송도컨벤시아) |
| 권호 | 17권 2호, p.1326 |
| 발표분야 | 공정시스템 |
| 제목 | Mathematical Modeling and Simulation for Vapor-Phase Cracking of Acetone process |
| 초록 | Chemical engineers need to model processes if they are going to design those devices and processes. Since the modeling of devices and phenomena is essential toengineering and science, chemical engineers have very practical reasons for doing mathematical modeling. Therefore, more and more chemicalengineers depend heavily on mathematical modeling. Many chemical engineering problems can be described by differential equations with known initial conditions, with known or given values of the state variables at the start of process. Numerical integration techniques generally suffice to solve initial value problems. This problems can be solved by using MATLAB. In this research, I considered a nonisothermal, nonadiabatic tubular reactor as a distributed systems. Object ofresearchis to find its steady-state concentration and temperature profiles. Specific process involves the vapor-phase cracking of aceton into ketone and methane, described by the endothermic reaction. |
| 저자 | 강병준, 박경태, 윤인섭 |
| 소속 | 서울대 |
| 키워드 | Mathematical Modeling |
| 원문파일 | 초록 보기 |
