American red cross swot analysis

CONTINUOUS DISTILLATIONCOLUMN - UOP3CC

A. INTRODUCTION TO THE EQUIPMENT

Distillation has always been and will continue to be one of the most important industrial processes for separating the different components of a liquid mixture. Laboratory scale distillation columns are needed to provide adequate practical training for student engineers and plant operators in a safe environment. They may also be used to acquire process separation data, of use in full-scale plant design.

The UOP3CC allows the study of both batch and continuous distillation, packed or plate column operation, operation under atmospheric pressure or under vacuum, azeotropic distillation, and manual, PID, PLC or computer control of the process. Data logging of the process is also possible.

UOP3CC Continuous Distillation Column

with computer control

Figure 1. Schematic Diagram of Apparatus

Figure 2. Diagram of Distillation Column

Figure 3. Diagram of UOP3CC Process Unit

Figure 4. Diagram of UOP3CC Console

B. DESCRIPTION

Where necessary, refer to the drawings on pages 19 to 22.

1. Overview

The UOP3CCContinuous Distillation Column is a self-contained distillation facility consisting of two interconnected units: a floor standing process unit and a bench mounted control console.

2. Floor-Standing Frame

The distillation column is mounted on a floor standing, welded tubular steel framework (1) fitted with four adjustable feet (2). The frame is designed to allow the use of a fork lift or pallet truck to manoeuvre the unit into position initially.

3. Distillation Column

The 50mm diameter sieve plate column is made up of two glass sections (3) and (4) each containing four sieve plates. The columns are separated by a central feed section and arranged vertically for counter-current vapor/liquid flow. The column is insulated to minimize heat loss.

The glass column incorporates a total of eight sieve plates in two sections (3) and (4) each containing four plates. Each plate (D) is located by a central support rod (E) and incorporates a weir (F) and downcomer (G) to create a liquid seal between successive stages. The liquid seal on the final plate in each section is achieved by U-tube (H).

Feed mixture from either of the feed tanks is pumped by pump (7) to the base, centre or top of the distillation column at connections (A), (B) or (C) respectively. The feed pump incorporates a length of Viton rubber tubing. This tubing is suitable for all of the recommended test mixtures (see “Operational Procedures”). Where other test mixtures are being used, the suitability of this material must be checked.

4. Reboiler

The reboiler (13) situated at the base of the column is manufactured from 316 stainless steel and incorporates a flame-proof immersion type heating element. Either batch or continuous distillation can be carried out using this reboiler.

In continuous operation, valve (V1) is open and bottom product flows from the reboiler through the bottom product cooler (15) to the bottom product tank (9). It is possible to preheat the feed to the column by directing the feed through a spiral coil in the bottom product cooler where heat is transferred from product leaving the reboiler at the boiling point. When feeding cold feed directly to the column, the product from the reboiler is cooled in the bottom product cooler by circulating cold water through the spiral coil.

For batch operation, valve (V1) remains closed so that the reboiler can be filled with the initial charge (10 to 12 litres) of binary mixture. The column and reboiler are both insulated to minimize heat loss. A level sensor (17) inside the reboiler protects the heating element from overheating due to low operating level and a sight glass (18) allows the level in the reboiler to be observed.

5. Condenser

Vapor from the top of the column passes to a water-cooled, coil-in-shell condenser (8), which may be fitted with an insulated jacket to allow heat balances to be carried out.

The shell of the condenser incorporates a pressure relief valve (PRV1) to protect the system in the event of a blocked vent and cooling water failure. Cooling water enters the condenser at a regulated rate through a rotameter (FI1) and the flow rate is controlled by diaphragm valve (V5). A cooling water supply is connected to the inlet nozzle (19) and serves also to operate the vacuum pump (20) when operation at reduced pressure is required. Water supply to the vacuum pump is controlled by valve (V14), which must only be operated when valve (V5) is open.

6. Decanter

Condensate is collected in a glass decanter (11) (phase separator) which is bypassed for normal distillation experiments by opening valve (V10). When the decanter is in use (separation of two immiscible liquids as condensate), valve (V10) is closed so that the overflow (25) and underflow (26) pipes inside the vessel, can take effect.

With valve (V10) open, condensate from the condenser outlet passes directly through the decanter to the inlet of the reflux ratio control valve (12) which is a 3-way solenoid operated valve. Depending on the setting of the reflux timers, condensate is directed by the reflux valve either back to the top of the column or to the top product collecting vessel (10). When directed to the column, the reflux passes through a U-seal where a valve (V3) can be used for measuring boil-up rate or for draining the U-seal. The contents of the top product tank (10) can be drained into the reboiler (13) for re-use viavalve (V12).

7. Thermocouples

Temperatures within the system are monitored by fourteen thermocouple sensors (T1 to T14) located at strategic positions in the system. T1 to T8 are located in the column and measure the temperature of the liquid on each sieve plate. There are seventeen locations for the temperature sensors, three of which do not have sensors installed but which can be fitted with sensors moved from other, less relevant locations when necessary.

8. Manometer

The total pressure drop across the column is indicated on a U-tube manometer (P1) via appropriate tappings in the column fitted with isolating valves (V6) and (V7).

9. Product Receiver

All of the vessels in the system are connected to a common vent on the top product receiver. This vent is normally connected through a 4.0 m length of tubing to a fume cupboard or safe atmospheric vent outlet.

10. Vacuum Pump

Operation at reduced system pressures is achieved using the water powered vacuum pump (20). When in use, the flexible vent pipe from the common connection on the top product receiver is attached to the inlet of this vacuum pump at (23), and motive water admitted via valve (V14), which must only be operated when valve (V5) is open.

The level of vacuum is adjusted using needle valve (V15) and is indicated on pressuregauge (P1).

11. Control Console

The console is attached to the process unit by an umbilical cable which is of adequate length to allow the console to be positioned at least 2.0 m away (outside the “Zone 2” area). See the Safety section at the front of this manual, and the Specifications section on page 15.

The following pages provide a description of the console controls and connections.

Figure 5a. Console Controls and Connections

Figure 5b. Console Controls and Connections

The rear of the UOP3CC Console houses all cable connection glands, mains connections and DC connections. Two data ports are provided, a USB port for direct connection to a PC with Armfieldsoftware, and a 20-way signal output port, which provides voltage outputs for each of thesensor readings.

Figure 6b. Rear of UOP3CC Console

The rear panel also houses zero and span potentiometers for each of the thermocouples, inorder that the displays on the front of the console can be adjusted to read correctly.

C. OPERATION

Where necessary, refer to the drawings on pages 19 to 22 and to the console description beginning on page 25.

1. Warning!

The vacuum pump must never be started before opening valve (V5) to allow cooling water to the condenser (8). Failure to observe this will cause solvent to be discharged to the drain with the vacuum pump motive water.

2. Reflux Ratio Control

The reflux ratio timer on the control console is used to set the quantity and frequency of condensate returning to the distillation column. With the timer switched off, all of the condensate will be directed to the column (total reflux).

2.1. Typical reflux ratio examples

If the reflux ratio required is 2:1 and the total cycle time required is 21 seconds:

Condensate will be directed by the reflux ratio valve to the column for 14 seconds then to the top product receiver for 7 seconds. This cycle will then be repeated continuously until different values are inserted to the controller or until the reflux control is switched off.

If a ratio of 4:1 is required over the same cycle time:

Condensate will be directed to the column for 16.8 seconds and to the top product receiver for 4.2 seconds. The calculation is as follows:

4 + 1 = 5; 21/5 = 4.2; 4 x 4.2 = 16.8; (21 - 16.8 = 4.2)

2.2. Setting the controller

The time range and mode of the controller can only be set when the electrical supply to the controller from the control console is switched off.

Switch off the reflux controller switch on the control console. This switches off the power supply to the controller. The controller is now not controlling reflux flow. Because the controller has an internal battery, the display is still illuminated and the controller settings may be adjusted.

Press the SET button on the reflux ratio timer. The controller should be set to Immediate Cycle (CY) mode. If CY is not already set, use the D button to cycle through the modes until CY is displayed.

Press the SET key again.

Select the time range required. Seconds × 10 is suggested as the most suitable time range, allowing cycle times of between 00.1 and 99.9 seconds to be set. Use the D button to cycle through the modes until sec × 10 is displayed.

The set time may then be adjusted at any time (even when the controller is switched on), as follows (this assumes that secx10 mode has been selected):

Set the time interval during which condensate should be directed to the top product receiver (CY+ on the controller):

Press SET to select the 10 digit

Press D to set the 10 digit

Press SET to select the 1 digit

Press D to set the 1 digit

Press SET to select 0.1 digit

Press D to set the 0.1 digit

Set the time interval during which condensate should be directed back to the column (CY- on the controller):

Press SET to select the 10 digit

Press D to set the 10 digit

Press SET to select the 1 digit

Press D to set the 1 digit

Press SET to select 0.1 digit

Press D to set the 0.1 digit

Press SET to end time adjustment. To begin controller operation, switch on power to the reflux controller using the reflux controller on/off switch. The CY- digit in the bottom right of the display now indicates flow of condensate back to the column. The CY+ digit indicates flow of condensate to the top product tank. To display the set time during operation, press SET once to display set time CY+,twice to display set time CY-.

3. Measuring Temperatures

There are thirteen temperature sensing stations on the equipment, which are designated as follows:

T1 = Top tray of distillation column

T2 = 2nd tray

T3 = 3rd tray

T4 = 4th tray

T5 = 5th tray

T6 = 6th tray

T7 = 7th tray

T8 = 8th tray

T9 = Temp of liquid in reboiler

T10 = Temp of vapor leaving the column above tray 1

T11 = Temp of cooling water entering condenser

T12 = Temp of cooling water leaving condenser

T13 = Temp of condensate as reflux/top product

T14 = Temp of feed liquid from feed tank

It is intended that both thermocouples T11 and T12, can be moved to any of the three positions marked T on the flow diagram. This will be necessary when carrying out a feed preheat experiment or an azeotropic distillation experiment.

In fact all of the thermocouples are identical so any can be moved to different locations but T11 and T12 are the recommended “movable” sensors as their connecting cables will not require any special re-routing. When moving sensors, always ensure that the blank fitting removed from the new sensor location is used to blank off the fitting from which the sensor was removed.

Temperatures may be viewed on the display on the right-hand panel of the control console. To display any temperature from T1 to T8, set the upper selector dial to the corresponding station designation. To display temperatures T9 to T14, turn the upper selector dial fully clockwise (to the furthest right-hand setting) and then set the lower selector dial to the station designation required.

4. Measuring Column Pressure Drop

The overall pressure drop over the column can be measured using the manometer P1. Always open V6 before V7, take the pressure reading then immediately close both valves. This will reduce the risk of contamination of the manometer water by the hydrocarbons.

Also to prevent contamination, never open valves V6 or V7 when flooding is occurring on the sieve plates (boil-up rate too high).

5. Taking Samples for Analysis

Samples for analysis can be taken from pertinent points in the system as follows:

Feed liquid - From feed tank

Liquid in reboiler - V2 (WARNING! Liquid at boiling point!)

Condensate from condenser - V3 (reflux/top product)

Top product receiver - V4

Bottom product receiver - V11

Note: When using valve V3 to obtain a sample of top product or to measure boil up rate the valve should not be fully opened, to prevent vapor from escaping. Gradually open valve V3 until flow of reflux into the column stops but liquid is retained in the flexible connecting pipe. Small adjustments of the valve position can be applied to maintain the desired level in the pipe. Provided that the same level in the pipe is maintained at the start and finish of the timing operation then the boil up rate measured will be accurate.

6. Feed Pump Calibration

The peristaltic feed pump is designed to give approximately 1 ml/min per revolution of the drive shaft. As the variable speed motor is capable of speeds varying from 0 to 300 RPM, the pump will be able to deliver approximately 0 to 300 ml/min of feed to the column.

In order to achieve greater accuracy, it is necessary to produce a calibration graph of the actual flow rate against the position of the variable speed dial on the control console. The dial has ten full turns, each full turn marked in one hundredth segments.

To produce the graph it will only be necessary to measure the flow at ten settings over the full range. Disconnect the feed tubing to the distillation column. Ensure the feed tank with the pump suction pipe inserted has sufficient water for the calibration. Using a 250 ml graduated cylinder and a stop watch, simply determine the flow rate at the ten settings and construct a graph which can be subsequently located near the control console.

Note: The distillation column has been designed for feed rates between 50 and 200 ml/min depending on the chemicals being used so a slight inaccuracy at the minimum and maximum settings of the pump speed will not affect the process.