Mixer and Splitter

Author: Nicklaus Dotzenrod ^[2015] Stewards: Jian Gong and Fengqi You

Introduction

The production of products from chemical processing plants usually involve a variety of mechanical equipment. Distillation columns, reactors, heaters and condensers are some of the most prominent pieces of equipment utilized at production facilities. Mixers and splitters, however, are equally important and play crucial roles in many different types of processes.

Mixers

Mixers play an important role in many different production processes, at the beginning or at the end. Some processes require several feed streams to be properly mixed before a reaction is commenced in a reactor. Other processes require that final products are blended together. Mixers serve to achieve both of these roles. Materials in all physical states are capable of being mixed together, whether it is gas mixing, liquid mixing, gas-liquid mixing or solid-liquid mixing.

Gas Mixing

In certain processes, gas to gas mixing is necessary to produce a desire product. This type of mixing is rare, however, as gases have low viscosity making them easy to mix on there own, without the assistance of a mechanical mixer. An example of gas mixing would be the mixing of oxygen, along with other gases to dilute the oxygen to desired compositions. Usually, a long pipe that contains turbulent airflow is sufficient enough to mix gases.

Liquid Mixing

Processes that require the mixing of two liquids are very common in many industries. Several factors should be considered when determining the type of mixer needed including the degree of mixing required, if the process is a batch or continuous operation and the properties of the liquids being mixed. There are several methods by which liquid to liquid mixing can be achieved.

1. Inline Mixing Inline mixers are static devices that provide a turbulent
   

   Figure 1 Inline Mixing Diagram
   environment that promote the mixing of liquids. They are generally inexpensive and can be used to mix both laminar and turbulent flows. There are several types of inline mixers.

• Tee Mixer Allows for two lower viscosity fluids to meet at an intersection where they are able to meet and exit the "tee" together.
• Injection Mixer Fluid is introduced into a stream of another fluid with a concentric pipe injector, allowing for mixing to occur via turbulent diffusion.
• Annual Injection Mixer Very similar to the injection mixer except fluid is introduced into another stream of fluid with an annular array of jets instead of a single concentric pipe.

1. Stirred Tanks Stirred tanks are mixing vessels equipped with an agitation device to promote the mixing of liquids. These mixers are quite often used for mixing viscous liquids.
   

   Figure 2 Stirred Tank Diagram
2. Side-entering Agitators
   

   Figure 3 Side-Entering Agitator Diagram

Gas-Liquid Mixing

There are several different types of mechanical mixers used to achieve a homogeneous gas-liquid mixture. Some include inline mixers, stirred vessels and other static mixers. A special device called a sparger can be used for this type of mixing as well. A sparger is essentially an injection tube with multiple holes in it to disperse gas within a tube filled with a liquid.

Solid-Liquid Mixing

There are times when a process requires a solid to mixed with a liquid. Generally, this is due to the fact the solids are insoluble and need to be transported as a slurry. Often times, stirred tanks are used to mix these physical states. Additionally, a screw conveyor can be used.

Aspen HYSYS Version 8.0 Simulation for Mixers

Aspen HYSYS software is an easy to use process modeling software that allows users to design efficient systems for industrial applications. HYSYS is capable of simulating many types of equipment that most industrial processes would require, including mixers. Unfortunately, HYSYS is only able to model a generic mixer, and is not able to model a specific model. The mixer used in HSYSY simulates and ideal mixing environment.

Preparing Simulation Environment

Before a mixer can be simulated, the HYSYS simulation environment must be prepared. The first step is to pick a fluid package. The package chosen is based on the materials being used and the overall process being simulated. The next step is to choose components. These also, depend on what type of process is being modeled.

Creating Input Streams

After a fluid package and components have been chosen, steams can be entered into the simulation environment. For the example shown in Figure 1., only two input steams are used.

Figure 1 Creating Input Streams

Specify Input Streams

After creating the input steams, they must be specified.

1. Click the Home tab at the top of the screen.
2. Click the Workbook tab at the top of the screen.
3. Specify all known conditions of the input streams.

Figure 2 Specify Input Streams

Set Compositions of Streams

Set the compositions of the input streams by clicking on the Compositions tab located at the bottom of the Workbook. In the example shown in Figure 3, one stream is pure ethanol and one is pure water.

Figure 3 Set Compositions of Streams

Insert Mixer

To add a mixer to the simulation environment, look at the Palette tool box and find the Mixer component icon (illustrated in Figure 4). Now, the mixer can be placed onto the simulation environment, ideally near the two input streams already placed.

Figure 4 Insert Mixer

Connecting Mixer

Now that the mixer is placed into the simulation environment, it must be connect to input and output streams in order to function. Figure 5 illustrates the necessary steps.

1. Click the Flowsheet/Modify tab at the top of the screen.
2. Choose the Attach (paper clip) icon
3. Click and drag the two input streams and connect them to the mixer
4. Click the output side of the mixer and drag out an output stream

Figure 5 Connecting Mixer

Finalize Output Stream

Once all the input and output streams have been connected to the mixer, go back to the Home tab and click the workbook icon as illustrated in Figure 6. The output stream should be specified and should be well mixed representation of streams 1 and stream 2.

Figure 6 Finalize Output Stream

References

1. G.P. Towler, R. Sinnott, Chemical Engineering Design: Principles, Practice and Economics of Plant and Process Design, Elsevier, 2012.

2. Aspen HYSYS. Vers. 8. Bedford: AspenTech, 2014. Computer software.