Comparative Study of PID Controllers for Time-Varying of Steam Distillation Process

2021 ◽  
Author(s):  
Haslizamri Md Shariff ◽  
Mohd Hezri Fazalul Rahiman ◽  
Ramli Adnan ◽  
Mohd Hezri Marzaki ◽  
Mazidah Tajjudin ◽  
...  
Keyword(s):  
Comparative Study ◽  
Steam Distillation ◽  
Pid Controllers ◽  
Time Varying ◽  
Distillation Process

The Comparative Study of Anti-Windup PID Controllers for Steam Distillation Process

2020 ◽  
Author(s):  
Haslizamri Md Shariff ◽  
Mohd Hezri Fazalul Rahiman ◽  
Ramli Adnan ◽  
Mohd Hezri Marzaki ◽  
Mazidah Tajjudin ◽  
...  
Keyword(s):  
Comparative Study ◽  
Steam Distillation ◽  
Pid Controllers ◽  
Distillation Process ◽  
The Comparative Study

scholarly journals Innovation in a Continuous System of Distillation by Steam to Obtain Essential Oil from Persian Lime Juice (Citrus latifolia Tanaka)

Molecules ◽  
2021 ◽  
Vol 26 (14) ◽  
pp. 4172
Author(s):  
José Daniel Padilla-de la Rosa ◽  
Magaly Dyanira Manzano-Alfaro ◽  
Jaime Rosalío Gómez-Huerta ◽  
Enrique Arriola-Guevara ◽  
Guadalupe Guatemala-Morales ◽  
...  
Keyword(s):  
Essential Oil ◽  
Oil Recovery ◽  
Steam Distillation ◽  
Optical Rotation ◽  
Process Time ◽  
Chemical Compositions ◽  
Distillation Process ◽  
Steam Consumption ◽  
Lime Juice ◽  
Oil Fractions

The citrus industry is one of the most important economic areas within the global agricultural sector. Persian lime is commonly used to produce lime juice and essential oil, which are usually obtained by batch distillation. The aim of this work was to validate a patented continuous steam distillation process and to both physically and chemically characterize the volatile fractions of essential Persian lime oil. Prior to distillation, lime juice was obtained by pressing the lime fruit. Afterwards, the juice was subjected to a continuous steam distillation process by varying the ratio of distillate flow to feed flow (0.2, 0.4, and 0.6). The distillate oil fractions were characterized by measuring their density, optical rotation, and refractive index. Gas chromatography GC-FID was used to analyze the chemical compositions of the oil fractions. The process of continuous steam distillation presented high oil recovery efficiencies (up to 90%) and lower steam consumption compared to traditional batch process distillation since steam consumption ranged from 32 to 60% for different steam levels. Moreover, a reduction in process time was observed (from 8 to 4 h). The oil fractions obtained via continuous steam distillation differed significantly in their composition from the parent compounds and the fractions.

Simulation of steam distillation process using neural networks

2009 ◽  
Vol 87 (8) ◽  
pp. 997-1002 ◽  
Author(s):  
M.T. Vafaei ◽  
R. Eslamloueyan ◽  
Sh. Ayatollahi
Keyword(s):  
Neural Networks ◽  
Steam Distillation ◽  
Distillation Process

Prediction of time-varying maximum scour depth around short abutments using soft computing methodologies - A comparative study

2015 ◽  
Vol 20 (5) ◽  
pp. 2070-2081 ◽  
Author(s):  
Khosrow Hosseini ◽  
Hojjat Karami ◽  
Hossein Hosseinjanzadeh ◽  
Abdollah Ardeshir
Keyword(s):  
Comparative Study ◽  
Soft Computing ◽  
Scour Depth ◽  
Time Varying ◽  
Computing Methodologies

Fast Pyrolysis of Distillated Ashe Juniper Biomass

2006 ◽  
Author(s):  
Jaime J. Jua´rez ◽  
Victor R. Contreras ◽  
Gaston R. Haupert ◽  
Steven Hill ◽  
Daren E. Daugaard
Keyword(s):  
Essential Oils ◽  
Large Scale ◽  
Steam Distillation ◽  
Energy Content ◽  
Fast Pyrolysis ◽  
Distillation Process ◽  
Lower Heating Value ◽  
Bio Oil ◽  
Ashe Juniper ◽  
Liquid Yield

Ashe Juniper is one of three major species of juniper native to Texas. Communities of Ashe Juniper occupy over 8 million acres of Texas rangelands and are responsible for herbage reduction, which adversely impacts the livestock carrying capacity. Ashe Juniper wood contains aromatic liquids called essential oils, which are economically beneficial for the personal care products industry. In order to exploit this benefit Texarome, Inc. of Leaky, Texas uses a large-scale steam distillation process to extract aromatic liquids from Ashe Juniper. This process results in a large quantity of Ashe Juniper woodchip waste for which there is few uses. A moderate temperature process known as fast pyrolysis was used to convert steam-distillated Ashe Juniper into a liquid known as bio-oil. An average liquid yield of 40.8% is reported for steam-distillated Ashe Juniper biomass and an average liquid yield of 47.3% is reported Ashe Juniper biomass that has not undergone the steam distillation process. This work demonstrates that the energy content of steam distillated Ashe Juniper can be extracted and the conversion to bio-oil is another potential use for Ashe Juniper woodchip waste. An economic model of Ashe Juniper biomass developed previously by Jua´rez and Daugaard was used to examine the economic impact of steam-distilled Ashe Juniper by simulating a 4,046-hectare (10,000 acre) Ashe Juniper energy plantation. It was found that bio-oil could be produced for as little as $5.20/GJ on a lower heating value basis if re-investment of profits made from the sale of essential oils extracted during the steam distillation process was assumed. Bio-oil from un-distillated Ashe Juniper could be produced for $13.21/GJ.

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