A Self-Tuning Regulator and a Feedforward Controller Based on Mass Balance to Control a Pilot-Scale Batch Distillation Column

1998 ◽  
Vol 31 (11) ◽  
pp. 619-624 ◽  
Author(s):  
Ronia M. Oisiovici ◽  
Sandra L. Cruz ◽  
João A.F.R. Pereira
Keyword(s):  
Mass Balance ◽  
Distillation Column ◽  
Pilot Scale ◽  
Batch Distillation ◽  
Self Tuning ◽  
Feedforward Controller

scholarly journals Dynamic-accumulative operation policy of continuous distillation for the purification of anisole

2016 ◽  
Vol 18 (1) ◽  
pp. 33-39
Author(s):  
Zhibo Wang ◽  
Shuairong Li ◽  
Caijiao Wang ◽  
Xianghai Guo ◽  
Peng Bai
Keyword(s):  
Flow Rate ◽  
Rate Control ◽  
Distillation Column ◽  
Operation Mode ◽  
Pilot Scale ◽  
Batch Distillation ◽  
Computer Codes ◽  
Great Sense ◽  
Flow Rate Control ◽  
Continuous Distillation

Abstract In the B10 isotope enrichment industry, the purification of anisole mixture makes great sense. A dynamic-accumulative operation policy of continuous distillation (DACD) with repeated filling and dumping of the still is proposed for the separation of trace heavy impurities in the recycled anisole. To simulate and optimize the purification process of anisole, a mathematical model of DACD is derived, and the computer codes are developed in the MATLAB environment. Moreover, the experiment is performed in a pilot-scale distillation column. The results show that the experimental date agrees well with simulation results. DACD could solve the difficulty of flow rate control when the bottom flow rate is very small in continuous distillation. The size of the still in this operation mode is also smaller than that in batch distillation. And the yield of anisole is raised to 99.91%. In a word, DACD is especially suitable for separating trace heavy impurities from the recycled anisole.

scholarly journals Approach Study for Mass Balance of Pesticide Residues in Distillers’ Stillage along with Distillate and Absence Verification of Pesticides in Distilled Spirits from Pilot-Scale of Distillation Column

Molecules ◽  
2019 ◽  
Vol 24 (14) ◽  
pp. 2572
Author(s):  
Jung-Ah Shin ◽  
Hoonho Cho ◽  
Dong-Woo Seo ◽  
Hee-Gon Jeong ◽  
Sung Chul Kim ◽  
...  
Keyword(s):  
Vapor Pressure ◽  
Mass Balance ◽  
Rice Bran ◽  
Pesticide Residues ◽  
Pilot Plant ◽  
Distillation Column ◽  
Pilot Scale ◽  
Distilled Spirits ◽  
High Vapor ◽  
Pilot Plant Scale

Herein, contaminants remaining in distillate and distillers’ stillage were quantitatively measured after distillation. After rice bran powder was contaminated with 10 ppm of lead (Pb) and cadmium (Cd) or 0.02–1.27 ppm of five pesticides (terbufos, fenthion, iprobenfos, flutolanil, and ethoprophos) followed by fermentation, single-stage distillation was performed. In the obtained distillate, no Pb or Cd was found, as expected. However, when the pesticides were added as contaminants, trace–0.05 ppm of some pesticides were detected in the distillate, possibly due to the high vapor pressure (e.g., that of ethoprophos) and contamination amount (e.g., that of flutolanil, terbufos, and fenthion). In contrast, none of the contaminating pesticides were observed in the distilled spirits when a fermented liquefaction contaminated with 0.04–4 ppm of six pesticides (fenthion, terbufos, ethoprophos, iprobenfos, oxadiazon, and flutolanil) was distilled using a pilot-plant scale distillation column, indicating that the pesticides hardly migrate to the distilled spirits.

Hydrolysis of organic wastewater particles in laboratory scale and pilot scale biofilm reactors under anoxic and aerobic conditions

1998 ◽  
Vol 38 (8-9) ◽  
pp. 179-188 ◽  
Author(s):  
K. F. Janning ◽  
X. Le Tallec ◽  
P. Harremoës
Keyword(s):  
Organic Matter ◽  
Mass Balance ◽  
Particulate Organic Matter ◽  
Removal Rate ◽  
Pilot Scale ◽  
Laboratory Scale ◽  
Synthetic Wastewater ◽  
Aerobic Conditions ◽  
Biofilm Reactors ◽  
Hydrolysis Of

Hydrolysis and degradation of particulate organic matter has been isolated and investigated in laboratory scale and pilot scale biofilters. Wastewater was supplied to biofilm reactors in order to accumulate particulates from wastewater in the filter. When synthetic wastewater with no organic matter was supplied to the reactors, hydrolysis of the particulates was the only process occurring. Results from the laboratory scale experiments under aerobic conditions with pre-settled wastewater show that the initial removal rate is high: rV, O2 = 2.1 kg O2/(m3 d) though fast declining towards a much slower rate. A mass balance of carbon (TOC/TIC) shows that only 10% of the accumulated TOC was transformed to TIC during the 12 hour long experiment. The pilot scale hydrolysis experiment was performed in a new type of biofilm reactor - the B2A® biofilter that is characterised by a series of decreasing sized granular media (80-2.5 mm). When hydrolysis experiments were performed on the anoxic pilot biofilter with pre-screened wastewater particulates as carbon source, a rapid (rV, NO3=0.7 kg NO3-N/(m3 d)) and a slowler (rV, NO3 = 0.3 kg NO3-N/(m3 d)) removal rate were observed at an oxygen concentration of 3.5 mg O2/l. It was found that the pilot biofilter could retain significant amounts of particulate organic matter, reducing the porosity of the filter media of an average from 0.35 to 0.11. A mass balance of carbon shows that up to 40% of the total incoming TOC accumulates in the filter at high flow rates. Only up to 15% of the accumulated TOC was transformed to TIC during the 24 hour long experiment.

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