Mixer and Splitter: Difference between revisions
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Author: Nicklaus Dotzenrod<sup> [2015] </sup> | Author: Nicklaus Dotzenrod<sup> [2015] </sup> | ||
Stewards: Jian Gong and Fengqi You | Stewards: Jian Gong and Fengqi You | ||
<br> | <br> | ||
== Introduction == | == 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. | 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. | ||
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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. | 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 === | === 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.[[File:gasmixer.jpg|thumb|center|'''Figure 1''' Standard 2-Gas Mixer|150x150px]] | 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 (Towler and Sinnot, 2012).[[File:gasmixer.jpg|thumb|center|'''Figure 1''' Standard 2-Gas Mixer|150x150px]] | ||
=== Liquid Mixing === | === 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. | 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 (Towler and Sinnot, 2012). | ||
1.'''Inline Mixing''' Inline mixers are static devices that provide a turbulent [[File:108.jpg|thumb|right|none|'''Figure 2''' Inline Mixing Diagram|150x150px]] 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. | 1.'''Inline Mixing''' Inline mixers are static devices that provide a turbulent [[File:108.jpg|thumb|right|none|'''Figure 2''' Inline Mixing Diagram|150x150px]] 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. | ||
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=== Gas-Liquid Mixing === | === 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. [[File:sparger.jpg|thumb|center|'''Figure 5''' Diagram of a Sparger|250x250px]] | 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 (Towler and Sinnot, 2012). [[File:sparger.jpg|thumb|center|'''Figure 5''' Diagram of a Sparger|250x250px]] | ||
=== Solid-Liquid Mixing === | === 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. Typically, this sort of combination is mixed at atmospheric pressure with the completed mixture later being pumped at the process pressure[[File:screw.gif|thumb|center|'''Figure 6''' Screw Conveyor Animation|250x250px]] | 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. Typically, this sort of combination is mixed at atmospheric pressure with the completed mixture later being pumped at the process pressure (Towler and Sinnot, 2012).[[File:screw.gif|thumb|center|'''Figure 6''' Screw Conveyor Animation|250x250px]] | ||
== Aspen HYSYS Version 8.0 Simulation for Mixers== | == 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. | 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 (Aspen HYSYS, 2014). | ||
===Preparing Simulation 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. | 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. | ||
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[[File:material6.jpg|thumb|none|'''Figure 12''' Finalize Output Stream|800x800px]] | [[File:material6.jpg|thumb|none|'''Figure 12''' Finalize Output Stream|800x800px]] | ||
== Conclusion == | |||
HYSYS does not offer a very comprehensive means of simulating a mixing process, however, it is able to estimate the result of multiple material streams being mixed. The results of a mixing simulation in HYSYS should not be the sole simulation used when designing a process that includes mixing, but it will assist in determining general process dynamics. | |||
==References== | ==References== | ||
1. G.P. Towler, R. Sinnott, Chemical Engineering Design: Principles, Practice and Economics of Plant and Process Design, Elsevier, 2012. | 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. | 2. Aspen HYSYS. Vers. 8. Bedford: AspenTech, 2014. Computer software. |
Latest revision as of 05:15, 6 March 2015
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 (Towler and Sinnot, 2012).
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 (Towler and Sinnot, 2012).
1.Inline Mixing Inline mixers are static devices that provide a turbulent
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.
2.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. There are several types of agitators sued for stirred tanks including turbine impellers, pitched bladed turbine, paddle, anchor and helical ribbon.
3.Side-entering Agitators Side-entering agitators are useful for mixing lower viscosity fluids in larger tanks as these sort of tanks are not very compatible for top supported agitators.
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 (Towler and Sinnot, 2012).
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. Typically, this sort of combination is mixed at atmospheric pressure with the completed mixture later being pumped at the process pressure (Towler and Sinnot, 2012).
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 (Aspen HYSYS, 2014).
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 7., only two input steams are used.
Specify Input Streams
After creating the input steams, they must be specified.
- Click the Home tab at the top of the screen.
- Click the Workbook tab at the top of the screen.
- Specify all known conditions of the 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 9, one stream is pure ethanol and one is pure water.
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 10). Now, the mixer can be placed onto the simulation environment, ideally near the two input streams already placed.
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 11 illustrates the necessary steps.
- Click the Flowsheet/Modify tab at the top of the screen.
- Choose the Attach (paper clip) icon
- Click and drag the two input streams and connect them to the mixer
- Click the output side of the mixer and drag out an output stream
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 12. The output stream should be specified and should be well mixed representation of streams 1 and stream 2.
Conclusion
HYSYS does not offer a very comprehensive means of simulating a mixing process, however, it is able to estimate the result of multiple material streams being mixed. The results of a mixing simulation in HYSYS should not be the sole simulation used when designing a process that includes mixing, but it will assist in determining general process dynamics.
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.