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A packed column distillation process experiment was conducted with the goal of understanding the operation of vapourliquid separation, analyzing the sample for the top and bottom product by refractometer to obtain the refractive index (RI) in order to determine their respective composition and also to obtain the time when the vapourliquid separation is nearly finish. In this experiment 30 litres of 10% v/v (volume/volume) mixture of Ethanol in water was prepared and filled in a reboiler vessel. The mixture was allowed to boiled until almost all component with low boiling point has been vaporized from the mixture.
Distillation is a separation process where liquid or vapor mixture of two or more substance is separated into its desired component fractions through boiling and condensation. In this experiment, mixture of methylcyclohexane (MCH) and toluene were used. This experiment was conducted to determine pressure drop for various boil-up rates in a batch distillation, the degree of foaming on trays each time the power increased and the measurement of Refractive Index. There are two parts of experiments were conducted which were determining pressure drop in batch distillation and determining unknown concentration. With the aim of getting pressure drop of the column, the power was set up to 0.5kW, 0.75kW, 1.00kW, and 1.25kW. For every power, 100mL of sample was collected to measure the Refractive Index. It is observed the degree of foaming was increased with the increment of power. For experiment B, pure MCH, pure toluene, 25% MCH, 50% MCH and 75% MCH were tested for their Refractive Index to compare the value with the previous sample from experiment A. It can be concluded that this experiment has achieved its objectives which is the boil-up rates depend on the heater power used. The greater the heater power, the higher the boil-up rates will be and the refractive index values shows an increment when the power input increase. Turnitin : Percentage Similarity (15%)
2016
Distillation used in large number of industry in the world as purification unit. Distillation unit has two kind of separation column, plate and packing. Distillation unit in this research use packing as separation coloumn and type of packing is glass raschig ring. Dimension of distillation unit are; 1.20 m on height, 45 mm on diameter, 2 mm on wall thikness. dimensions of one glass raschig rings are; 0.5 mm of out diameter, 8.5 mm on lenght, 0.85 mm on wall thickness and 19.5 cm on high of packing. High Equivalent of Theoritical Plate (HETP) is a methode to calculate how many plate that equivalent to the high of packing. Both fenske underwood and mc-cabe thiele methode was used to calculate the HETP. Data from ethanol purification with different input concentration collected to calculate the HETP. Different concentration of ethanol; 50%, 55%, 60%, 65% and 70% used as input in distillation process. Sample of distillat and bottom took in 76 0C and 82 0C. Concentration of distillat and...
This project investigates the challenges being faced by science and engineering students of Federal Polytechnic Ado-Ekiti, Nigeria in carrying out experiments in the laboratories. It proffers a solution to eliminate some of the challenges by fabricating an improved scientific glass apparatus for water distillation. The project also highlights the significance of water distillation to laboratories, the process of distillation and distillation rate, and the scientific glass-working operations and techniques. The latter chapter discusses the materials and methodology adopted for the apparatus fabricated. Moreover, conclusion was derived and recommendation proffered.
The Online Journal of Science and Technology, 2012
There have been relatively few experimental attempts at evaluating the column height and comparing experimental results obtained from a pilot scale packed batch distillation column with theoretical ones. In the present study, the pilot plant packed batch distillation column was used to distillate the binary methanol-water mixture, and to obtain on-line temperature values. The top temperature changes with time were observed at steady-state and dynamic conditions. The column was operated initially for approximately one hour at the total reflux. In this case, There were no feed and product flows. Temperature samples were taken on-line from the top and bottom of the column. Temperature profiles observed on the computer were recorded. Refractive index of the samples were determined. When the temperatures were constant, the system was at a steady-state condition for total reflux. After the system reached the steady-state condition the reflux ratio was adjusted to a certain level. From exp...
Hemijska industrija, 2006
For distillation column design it is necessary to define all the variable parameters such as component concentrations in different streams temperatures, pressures, mass and energy flow, which are used to represent the separation process of some specific system. They are related to each other according to specific laws, and if the number of such parameters exceeds the number of their relationships, in order to solve a problem some of them must be specified in advance or some constraints assumed for the mass balance, the balance of energy, phase equilibria or chemical equilibria. Knowledge of specific elements which are the constituents of a distillation unit must be known to define the number of design parameters as well as some additional apparati also necessary to realize the distilation. Each separate apparatus might be designed and constructed only if all the necessary and variable parameters for such a unit are defined. This is the right route to solve a distilation unit in many...
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