Vacuum distillation
The aim of this report is to investigate the potential advantages and disadvantages of shifting from atmospheric distillation to vacuum distillation in neutral alcohol production.
1. Atmospheric pressure
First, the current configuration of alcohol production is presented. The current configuration of alcohol production at distillery site, Barossa Valley, consists of 4 main columns, wash column-1, rectifier, methanol column-1 and methanol column-2. Figure-1, Schematic of the neutral alcohol production at distillery site.
All columns are operated near atmospheric pressure and a brief overview of the main streams composition and alcohol strength can be found in table-1. The summary of required utilities at atmospheric
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(oC) 81.2 80.7 78.5 - -
Reboiler duty (kW) - 2006 600 600 3206
Steam (kg/hr) 7500 3366 1007 1007 12880
2. Vacuum pressure at 8-5 kPa
The current configuration of columns at distillery site has been simulated at vacuum of 8-5 kPa, in which the first number represents the column bottom pressure and the second one shows the column top pressure for WC-1, MC-1 & 2. The results are shown in tables-3 and 4.
Table-3, Composition and alcohol strength at current configuration, vacuum 8-5 kPa
Case-2, Current configuration, vacuum 8-5 kPa, stream compositions
Stream name
Composition WC-1 Feed WC-1 Bottom WC-1 Head HydroSelec. H2O REC-Spirit Final Product ppm (mg/L) ppm (mg/L) ppm (mg/L) ppm (mg/L) ppm (mg/L) ppm (mg/L)
Water (%abv) 53.68 88.79 10.97 97.04 4.04 4.07
Ethanol (%abv) 45.84 11.09 86.26 2.88 95.71
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(oC) 18 80.7 17.2 - -
Reboiler duty (kW) - 3371 400 400 4171
Steam (kg/hr) 7500 5655 0* 0* 10886
*The required heat is supplied through the REC condenser.
The results show that there is not a significant change in the process streams and the final product. However, table-4 shows a considerable saving in steam consumption. That is because the required heat load for MC-1 & 2 is provided by REC condenser. The condenser loads has slightly increased. Having said that this situation is not possible as the condenser temperatures for WC-1 and MC-1 are below wet bubble temperature, 20oC for the plant location.
3. Vacuum pressure at 20-15
This report is based on the plant information of Jos. Schlitz Brewing Company's sixth brewery, which located near Winston- Salem, North Carolina. The purpose of this report is to show the brewery's operation management, analysis and critique the plans and actions of the organization, and point out some disadvantages in the operating.
A small beaker was placed under the arm of the distillation head to catch the distillate. Foil was wrapped around the neck of the round-bottomed flask and a wet paper towel was wrapped around the arm of the distillation head to create a condenser. The flask was heated gently so that the distillate dropped at a rate of two drops per minute. The temperature was recorded as every drop was collected. The distillation began at around 55.0 ℃. The distillation was stopped after 29 drops were collected to prevent the solution from being distilled to dryness. See attached data. The known boiling point of 1-butanol is 117.5 ℃ (Lemonds). The known boiling point of 1-propanol is 97 ℃ (Thiyagarajan). The known boiling point of acetone is 56 ℃ (Forss). The known boiling point of 2-butanone is 79.6 ℃ (Jiang). For unknown #3 the boiling point of the first substance seemed to be around 56 ℃ and the boiling point of the second substance seemed to be around 111 ℃. Therefore unknown #3 seemed to be a mixture of acetone and 1-butanol.
Simple distillation is a separation technique which can be used to separate and purify distillates from a liquid mixture which ideally contains one volatile and one non-volatile compound. If such ideal conditions are not possible—as is usually the case—then simple distillation can be applied as long as the liquid in question is composed of compounds that differ in volatility such that their boiling points differ by at least 40 to 50 degrees Celsius. Because
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The memo summarizes the findings from the initial assessment performed on the 190 proof SDA-3AU alcohol for use in Fractionation and downstream processes.
Based on the small Scottish island of Islay, John Jonston is credited as the founder of the first legal distillery on the site. With an abundance of peat on the island, Lagavulin’s water originates from the Solum Lochs and filters through this rich peat towards the distillery. Due to the high quality of this water it has been subject to numerous legal battles with neighbouring distilleries to secure exclusive use.
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The objective of the lab was to purify compounds that can be turned into gas at a reasonable temperature without using decomposition. Gas chromatography was also used to identify the proportions of the volatile compound in the different samples. The mixture of hexane and octane was assigned to me and my partner. The apparatus for simple distillation was assemble using a thermocouple, air condenser, distillation head, metal keck clamps, and a conical reaction vial. The joints of the glassware were greased before assembly. Four boiling chips were placed in the conical ration vial before it was assembled. After being assigned a mixture, 3.5 mL of the mixture was put into a reaction vial. The apparatus
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