This paper concerns techno-economic optimization of the production process of raw ethanol in a continuous distillation column as a part of the plant for production of rectified alcohol. Optimization was performed in order to determine the optimal ethanol concentration in the residue, which provides the minimum total production costs of existing plant. Total production costs are determined on the basis of experimental data, investment and operating costs and the estimated working life of the plant. It was found that ethanol concentration in the residue is significantly higher than values that can be found in the open literature
Process Design for the Production of Ethylene from Ethanol This project considers using ethanol dehy...
[[abstract]]Several common ethanol fuel mixtures (E3-E85) are in use around the world. Ethanol fuel ...
An industrial de-alcoholizing plant and a distillation column were designed, for processing 0.56 kg/...
This paper concerns techno-economic optimization of the production process of raw ethanol in a conti...
This paper presents the techno-economic optimization of batch plant for production of rectified alco...
This paper presents the techno-economic optimization of batch plant for production of rectified alco...
In order for ethanol to be competitive with gasoline, the production cost of ethanol must be lower t...
Process simulation was used to analyze bioethanol distillation process, which requires a large amoun...
The purpose of the project was to design, fabricate, and evaluate a small scale continuous ethanol p...
As a result of actual pilot experimental data and guided by international and national reported esti...
The 2nd generation plants producing ethanol from lignocelluloses demand risky and high investment co...
The 2nd generation plants producing ethanol from lignocelluloses demand risky and high investment co...
The 2nd generation plants producing ethanol from lignocelluloses demand risky and high investment co...
The 2nd generation plants producing ethanol from lignocelluloses demand risky and high investment co...
A techno-economic analysis on the production of cellulosic ethanol by fermentation was conducted to ...
Process Design for the Production of Ethylene from Ethanol This project considers using ethanol dehy...
[[abstract]]Several common ethanol fuel mixtures (E3-E85) are in use around the world. Ethanol fuel ...
An industrial de-alcoholizing plant and a distillation column were designed, for processing 0.56 kg/...
This paper concerns techno-economic optimization of the production process of raw ethanol in a conti...
This paper presents the techno-economic optimization of batch plant for production of rectified alco...
This paper presents the techno-economic optimization of batch plant for production of rectified alco...
In order for ethanol to be competitive with gasoline, the production cost of ethanol must be lower t...
Process simulation was used to analyze bioethanol distillation process, which requires a large amoun...
The purpose of the project was to design, fabricate, and evaluate a small scale continuous ethanol p...
As a result of actual pilot experimental data and guided by international and national reported esti...
The 2nd generation plants producing ethanol from lignocelluloses demand risky and high investment co...
The 2nd generation plants producing ethanol from lignocelluloses demand risky and high investment co...
The 2nd generation plants producing ethanol from lignocelluloses demand risky and high investment co...
The 2nd generation plants producing ethanol from lignocelluloses demand risky and high investment co...
A techno-economic analysis on the production of cellulosic ethanol by fermentation was conducted to ...
Process Design for the Production of Ethylene from Ethanol This project considers using ethanol dehy...
[[abstract]]Several common ethanol fuel mixtures (E3-E85) are in use around the world. Ethanol fuel ...
An industrial de-alcoholizing plant and a distillation column were designed, for processing 0.56 kg/...