Terminal control algorithm for the downrange motion of a descent module with load factor constraints

2012 ◽  
Vol 51 (5) ◽  
pp. 715-731 ◽  
Author(s):  
S. N. Evdokimov ◽  
S. I. Klimanov ◽  
A. N. Korchagin ◽  
E. A. Mikrin ◽  
Yu. G. Sikharulidze
2020 ◽  
Vol 58 (2) ◽  
pp. 122-137
Author(s):  
S. N. Evdokimov ◽  
S. I. Klimanov ◽  
A. N. Korchagin ◽  
E. A. Mikrin ◽  
A. S. Samotokhin ◽  
...  

2018 ◽  
pp. 1-27 ◽  
Author(s):  
Yury Georgievich Sikharulidze ◽  
Andrey Nikolaevich Korchagin ◽  
Alexander Sergeevich Samotokhin ◽  
Andrey Georgievich Tuchin

2012 ◽  
Vol 51 (6) ◽  
pp. 802-817 ◽  
Author(s):  
S. N. Evdokimov ◽  
S. I. Klimanov ◽  
A. N. Korchagin ◽  
E. A. Mikrin ◽  
Yu. G. Sikharulidze
Keyword(s):  

2019 ◽  
Vol 57 (3) ◽  
pp. 176-187 ◽  
Author(s):  
S. N. Evdokimov ◽  
S. I. Klimanov ◽  
A. N. Korchagin ◽  
E. A. Mikrin ◽  
A. S. Samotokhin ◽  
...  

2015 ◽  
Vol 2 (1) ◽  
pp. 6-12
Author(s):  
Agus Sugiarta ◽  
Houtman P. Siregar ◽  
Dedy Loebis

Automation of process control in chemical plant is an inspiring application field of mechatronicengineering. In order to understand the complexity of the automation and its application requireknowledges of chemical engineering, mechatronic and other numerous interconnected studies.The background of this paper is an inherent problem of overheating due to lack of level controlsystem. The objective of this research is to control the dynamic process of desired level more tightlywhich is able to stabilize raw material supply into the chemical plant system.The chemical plant is operated within a wide range of feed compositions and flow rates whichmake the process control become difficult. This research uses modelling for efficiency reason andanalyzes the model by PID control algorithm along with its simulations by using Matlab.


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