This document provides information on various types of structured packing solutions from GTC Technology. It begins with an introduction to structured packing and then describes different product lines including GT-PAK for conventional structured packing, GT-OPTIM PAK for high capacity structured packing, and GT-AQUA PAK for aqueous services. Graphs are included comparing the performance of structured packing to random packing in terms of efficiency, capacity, pressure drop and other factors. The document contains technical details on material properties and performance characteristics for proper selection of structured packing products.
Equilibrium Effects
- Methane Steam
- Water Gas Shift
Relationship of Kp to Temperature
Relationship of WGS Kp to Temperature
Effect of Temperature on Methane Slip
Approach to Equilibrium
Reaction Path and Equilibrium
Effect of Pressure Increase
Operating Parameters
- Pressure
- Temperature
- Feed Rate
- Steam to Carbon
Effect of Exit Temperature Spread
Useful Tools
Calculating ATM
Look at two main types
Explain mechanisms
Explain prevention of cracking
Three main types
1 Carbon cracking
2 Boudouard carbon formation
3 CO reduction
1. Introduction reasons for purification, types of poisons, and typical systems
2. Hydrogenation
3. Dechlorination
4. Sulfur Removal
5. Purification system start-up and shut-down
Introduction and Theoretical Aspects
Catalyst Reduction and Start-up
Normal Operation and Troubleshooting
Shutdown and Catalyst Discharge
Nickel Carbonyl Hazard
Modern Methanation Catalyst Requirements
Installation of S-50 ammonia synthesis converter along with waste heat boiler in downstream of existing S-200 ammonia synthesis converter is one of the major schemes of Energy Saving Project of Ammonia plant. The energy saving reported 0.18 G.Cal/T of Ammonia. Several ammonia plants have installed an additional ammonia synthesis converter in combination with a HP steam waste heat boiler, downstream of the existing ammonia converter. The result is increased conversion per pass, reduced compression requirements due to the smaller recycle gas stream, and improved waste heat recovery. Among the methodologies aimed at finding energy saving opportunities, pinch analysis linked to power and steam modeling has proved to be a powerful way for determining projects to improve the overall energy efficiency of industrial sites. This procedure has been applied successfully in many industrial facilities, allowing optimal energy recovery in the process and hence reduction of fuel consumption.
Rotary kiln design is a complex process, with a variety of factors and material characteristics influencing the sizing and design. This presentation gives an overview of the sizing and design process, including the many factors that will need to be considered during the design stage.
Equilibrium Effects
- Methane Steam
- Water Gas Shift
Relationship of Kp to Temperature
Relationship of WGS Kp to Temperature
Effect of Temperature on Methane Slip
Approach to Equilibrium
Reaction Path and Equilibrium
Effect of Pressure Increase
Operating Parameters
- Pressure
- Temperature
- Feed Rate
- Steam to Carbon
Effect of Exit Temperature Spread
Useful Tools
Calculating ATM
Look at two main types
Explain mechanisms
Explain prevention of cracking
Three main types
1 Carbon cracking
2 Boudouard carbon formation
3 CO reduction
1. Introduction reasons for purification, types of poisons, and typical systems
2. Hydrogenation
3. Dechlorination
4. Sulfur Removal
5. Purification system start-up and shut-down
Introduction and Theoretical Aspects
Catalyst Reduction and Start-up
Normal Operation and Troubleshooting
Shutdown and Catalyst Discharge
Nickel Carbonyl Hazard
Modern Methanation Catalyst Requirements
Installation of S-50 ammonia synthesis converter along with waste heat boiler in downstream of existing S-200 ammonia synthesis converter is one of the major schemes of Energy Saving Project of Ammonia plant. The energy saving reported 0.18 G.Cal/T of Ammonia. Several ammonia plants have installed an additional ammonia synthesis converter in combination with a HP steam waste heat boiler, downstream of the existing ammonia converter. The result is increased conversion per pass, reduced compression requirements due to the smaller recycle gas stream, and improved waste heat recovery. Among the methodologies aimed at finding energy saving opportunities, pinch analysis linked to power and steam modeling has proved to be a powerful way for determining projects to improve the overall energy efficiency of industrial sites. This procedure has been applied successfully in many industrial facilities, allowing optimal energy recovery in the process and hence reduction of fuel consumption.
Rotary kiln design is a complex process, with a variety of factors and material characteristics influencing the sizing and design. This presentation gives an overview of the sizing and design process, including the many factors that will need to be considered during the design stage.
(HTS) High Temperature Shift Catalyst (VSG-F101) - Comprehensiev OverviewGerard B. Hawkins
The high temperature shift duty introduction and theory
HTS catalyst characteristics
developments over time
Typical HTS operational problems
Improved catalysts
VULCAN Series VSG-F101 Series
Summary
Reformer Tube design principles
- Larsen Miller Plot
- Larsen Miller & Tube Design
- Design Margins - Stress Data Used
- Max Allowable & Design Temperature
- Tube Life
- Effect of Temperature on Life
- Material Types
HK40: 25 Cr / 20 Ni
HP Modified: 25 Cr / 35 Ni + Nb
Microalloy: 25 Cr / 35 Ni + Nb + Ti
- Alloy Developments
- Comparison of Alloys
Manufacturing Technology
- Welds
Failure mechanisms
- Failure Mechanisms - Creep
- Creep Propagation
- Common Failure Modes
- Uncommon Failure Modes
- Failure by Creep
- Creep Rupture - Cross Section
- Failure at Weld
Actions to Take if Tube Fails
- Pigtail Nipping
Inspection techniques
Classification of Problems
- Visual Examination
- Girth Measurement
- Ultrasonic Attenuation
- Radiography
Eddy Current Measurement
LOTIS Tube Inspection
LOTIS Compared to External Inspection
Catalytic Reforming Process is one of the most important processes in the petroleum and petrochemical industries which produce high octane number gasoline.
Common poisons include
Sulfur
Chlorides and other halides
Metals including arsenic, vanadium, mercury, alkali metals (including potassium)
Phosphates
Organo-metalics
Improve fired heaters performance and reliabiltyAshutosh Garg
Fired heaters are often suffering from high tube metal temperatures and short run lengths. Operators are always worried about hot spots in the furnace. While refineries want to push the heaters hard, the heater starts coking up and very soon, the heater tubes have to be cleaned.
FIS has done extensive research and CFD modelling of heaters in the recent time and has concluded that localized burner flame and hot flue gas currents are responsible for the hot spots on the tubes. FIS has now developed a new patented technology for solving hot spot problems. This technology called Inclined Firing Technology involves orienting the burners at an angle on the floor / wall/ roof to direct the flame away from the tubes. The results of this technology have been extremely good and with a very low investment, the reliability and run length of the heater is improved significantly.
Synthesis Gas and Refinery Hydrogen Applications
Support balls or more accurately, support balls and hold-down balls will at times need to be specified to our customers. Advice may also be needed opposite the usage of meshes and hold-down screens. This brief report focuses on some key aspects to consider.
1. Support Balls
2. Hold-down Balls
3. Meshes over Exit Collector & Exit Screen
4. Hold-down Screens
5. Support and Hold-down Ball Compositions and Applications
6. High Surface Area Dust Collectors
Introduction
reasons for purification, types of poisons, and typical systems
2. Hydrogenation
3. Dechlorination
4. Sulfur Removal
5. Purification system start-up and shut-down
This presentation covers process safety considerations and when a dynamic simulation is required. We also provide a modelling approach and a case study on Coker Bottoms Steam Generator, which includes information on device selection and device sizing.
(HTS) High Temperature Shift Catalyst (VSG-F101) - Comprehensiev OverviewGerard B. Hawkins
The high temperature shift duty introduction and theory
HTS catalyst characteristics
developments over time
Typical HTS operational problems
Improved catalysts
VULCAN Series VSG-F101 Series
Summary
Reformer Tube design principles
- Larsen Miller Plot
- Larsen Miller & Tube Design
- Design Margins - Stress Data Used
- Max Allowable & Design Temperature
- Tube Life
- Effect of Temperature on Life
- Material Types
HK40: 25 Cr / 20 Ni
HP Modified: 25 Cr / 35 Ni + Nb
Microalloy: 25 Cr / 35 Ni + Nb + Ti
- Alloy Developments
- Comparison of Alloys
Manufacturing Technology
- Welds
Failure mechanisms
- Failure Mechanisms - Creep
- Creep Propagation
- Common Failure Modes
- Uncommon Failure Modes
- Failure by Creep
- Creep Rupture - Cross Section
- Failure at Weld
Actions to Take if Tube Fails
- Pigtail Nipping
Inspection techniques
Classification of Problems
- Visual Examination
- Girth Measurement
- Ultrasonic Attenuation
- Radiography
Eddy Current Measurement
LOTIS Tube Inspection
LOTIS Compared to External Inspection
Catalytic Reforming Process is one of the most important processes in the petroleum and petrochemical industries which produce high octane number gasoline.
Common poisons include
Sulfur
Chlorides and other halides
Metals including arsenic, vanadium, mercury, alkali metals (including potassium)
Phosphates
Organo-metalics
Improve fired heaters performance and reliabiltyAshutosh Garg
Fired heaters are often suffering from high tube metal temperatures and short run lengths. Operators are always worried about hot spots in the furnace. While refineries want to push the heaters hard, the heater starts coking up and very soon, the heater tubes have to be cleaned.
FIS has done extensive research and CFD modelling of heaters in the recent time and has concluded that localized burner flame and hot flue gas currents are responsible for the hot spots on the tubes. FIS has now developed a new patented technology for solving hot spot problems. This technology called Inclined Firing Technology involves orienting the burners at an angle on the floor / wall/ roof to direct the flame away from the tubes. The results of this technology have been extremely good and with a very low investment, the reliability and run length of the heater is improved significantly.
Synthesis Gas and Refinery Hydrogen Applications
Support balls or more accurately, support balls and hold-down balls will at times need to be specified to our customers. Advice may also be needed opposite the usage of meshes and hold-down screens. This brief report focuses on some key aspects to consider.
1. Support Balls
2. Hold-down Balls
3. Meshes over Exit Collector & Exit Screen
4. Hold-down Screens
5. Support and Hold-down Ball Compositions and Applications
6. High Surface Area Dust Collectors
Introduction
reasons for purification, types of poisons, and typical systems
2. Hydrogenation
3. Dechlorination
4. Sulfur Removal
5. Purification system start-up and shut-down
This presentation covers process safety considerations and when a dynamic simulation is required. We also provide a modelling approach and a case study on Coker Bottoms Steam Generator, which includes information on device selection and device sizing.
A saving of 70% on operational costs from day one: that is just one of the outcomes resulting from the implementation by Freezeserve, one of the most advanced cold stores in the United Kingdom, of a revolutionary solution from ORTEC and SPIE. “This investment in the latest automated storage technology offers a ‘man-less’‚ cost effective storage system using the latest palletizing technology”, comments Terry Haigh, Operations Director for Freezeserve.
The TIG Group is specialized in Total Site Solutions – single source solutions without cost - and
time consuming interfaces. Our team consists of experienced specialists from different fields of
expertise and our professionalism is founded on complete in-house project management.
Visit our website: www.tiggroup-mena.com
The largest exporters of vacuum bagging and composite tooling materials for prepreg/autoclave, resin infusion, and wet lay-up processes is Airtech Advanced Materials Group. With nearly 50 years of extrusion experience, Airtech is your local source for vacuum bagging materials, composite tooling producers, and 3D Print knowledge. For more details: https://airtech.com/
The companies of Altra Industrial Motion offer many critical drivetrain products utilized in papermaking, corrugated and printing machine applications including clutches, tensioning brakes, gear couplings and belted drives.
VRC (Vertical Reciprocating Conveyor) Lift - Dealer Training 2020rrailis
Learn the features and benefits of CIP's VRC lift models. This is a must-see for elevator dealers, material handling companies, and mezzanine manufacturers/resellers.
Hybrid optimization of pumped hydro system and solar- Engr. Abdul-Azeez.pdffxintegritypublishin
Advancements in technology unveil a myriad of electrical and electronic breakthroughs geared towards efficiently harnessing limited resources to meet human energy demands. The optimization of hybrid solar PV panels and pumped hydro energy supply systems plays a pivotal role in utilizing natural resources effectively. This initiative not only benefits humanity but also fosters environmental sustainability. The study investigated the design optimization of these hybrid systems, focusing on understanding solar radiation patterns, identifying geographical influences on solar radiation, formulating a mathematical model for system optimization, and determining the optimal configuration of PV panels and pumped hydro storage. Through a comparative analysis approach and eight weeks of data collection, the study addressed key research questions related to solar radiation patterns and optimal system design. The findings highlighted regions with heightened solar radiation levels, showcasing substantial potential for power generation and emphasizing the system's efficiency. Optimizing system design significantly boosted power generation, promoted renewable energy utilization, and enhanced energy storage capacity. The study underscored the benefits of optimizing hybrid solar PV panels and pumped hydro energy supply systems for sustainable energy usage. Optimizing the design of solar PV panels and pumped hydro energy supply systems as examined across diverse climatic conditions in a developing country, not only enhances power generation but also improves the integration of renewable energy sources and boosts energy storage capacities, particularly beneficial for less economically prosperous regions. Additionally, the study provides valuable insights for advancing energy research in economically viable areas. Recommendations included conducting site-specific assessments, utilizing advanced modeling tools, implementing regular maintenance protocols, and enhancing communication among system components.
6th International Conference on Machine Learning & Applications (CMLA 2024)ClaraZara1
6th International Conference on Machine Learning & Applications (CMLA 2024) will provide an excellent international forum for sharing knowledge and results in theory, methodology and applications of on Machine Learning & Applications.
About
Indigenized remote control interface card suitable for MAFI system CCR equipment. Compatible for IDM8000 CCR. Backplane mounted serial and TCP/Ethernet communication module for CCR remote access. IDM 8000 CCR remote control on serial and TCP protocol.
• Remote control: Parallel or serial interface.
• Compatible with MAFI CCR system.
• Compatible with IDM8000 CCR.
• Compatible with Backplane mount serial communication.
• Compatible with commercial and Defence aviation CCR system.
• Remote control system for accessing CCR and allied system over serial or TCP.
• Indigenized local Support/presence in India.
• Easy in configuration using DIP switches.
Technical Specifications
Indigenized remote control interface card suitable for MAFI system CCR equipment. Compatible for IDM8000 CCR. Backplane mounted serial and TCP/Ethernet communication module for CCR remote access. IDM 8000 CCR remote control on serial and TCP protocol.
Key Features
Indigenized remote control interface card suitable for MAFI system CCR equipment. Compatible for IDM8000 CCR. Backplane mounted serial and TCP/Ethernet communication module for CCR remote access. IDM 8000 CCR remote control on serial and TCP protocol.
• Remote control: Parallel or serial interface
• Compatible with MAFI CCR system
• Copatiable with IDM8000 CCR
• Compatible with Backplane mount serial communication.
• Compatible with commercial and Defence aviation CCR system.
• Remote control system for accessing CCR and allied system over serial or TCP.
• Indigenized local Support/presence in India.
Application
• Remote control: Parallel or serial interface.
• Compatible with MAFI CCR system.
• Compatible with IDM8000 CCR.
• Compatible with Backplane mount serial communication.
• Compatible with commercial and Defence aviation CCR system.
• Remote control system for accessing CCR and allied system over serial or TCP.
• Indigenized local Support/presence in India.
• Easy in configuration using DIP switches.
Sachpazis:Terzaghi Bearing Capacity Estimation in simple terms with Calculati...Dr.Costas Sachpazis
Terzaghi's soil bearing capacity theory, developed by Karl Terzaghi, is a fundamental principle in geotechnical engineering used to determine the bearing capacity of shallow foundations. This theory provides a method to calculate the ultimate bearing capacity of soil, which is the maximum load per unit area that the soil can support without undergoing shear failure. The Calculation HTML Code included.
HEAP SORT ILLUSTRATED WITH HEAPIFY, BUILD HEAP FOR DYNAMIC ARRAYS.
Heap sort is a comparison-based sorting technique based on Binary Heap data structure. It is similar to the selection sort where we first find the minimum element and place the minimum element at the beginning. Repeat the same process for the remaining elements.
NUMERICAL SIMULATIONS OF HEAT AND MASS TRANSFER IN CONDENSING HEAT EXCHANGERS...ssuser7dcef0
Power plants release a large amount of water vapor into the
atmosphere through the stack. The flue gas can be a potential
source for obtaining much needed cooling water for a power
plant. If a power plant could recover and reuse a portion of this
moisture, it could reduce its total cooling water intake
requirement. One of the most practical way to recover water
from flue gas is to use a condensing heat exchanger. The power
plant could also recover latent heat due to condensation as well
as sensible heat due to lowering the flue gas exit temperature.
Additionally, harmful acids released from the stack can be
reduced in a condensing heat exchanger by acid condensation. reduced in a condensing heat exchanger by acid condensation.
Condensation of vapors in flue gas is a complicated
phenomenon since heat and mass transfer of water vapor and
various acids simultaneously occur in the presence of noncondensable
gases such as nitrogen and oxygen. Design of a
condenser depends on the knowledge and understanding of the
heat and mass transfer processes. A computer program for
numerical simulations of water (H2O) and sulfuric acid (H2SO4)
condensation in a flue gas condensing heat exchanger was
developed using MATLAB. Governing equations based on
mass and energy balances for the system were derived to
predict variables such as flue gas exit temperature, cooling
water outlet temperature, mole fraction and condensation rates
of water and sulfuric acid vapors. The equations were solved
using an iterative solution technique with calculations of heat
and mass transfer coefficients and physical properties.
Overview of the fundamental roles in Hydropower generation and the components involved in wider Electrical Engineering.
This paper presents the design and construction of hydroelectric dams from the hydrologist’s survey of the valley before construction, all aspects and involved disciplines, fluid dynamics, structural engineering, generation and mains frequency regulation to the very transmission of power through the network in the United Kingdom.
Author: Robbie Edward Sayers
Collaborators and co editors: Charlie Sims and Connor Healey.
(C) 2024 Robbie E. Sayers
2. Introduction page 1
Structured Packing page 3
Packing Performance Graphs page 4
Industry Standard Corrugated Sheet Packing page 8
High Capacity Structured Packing page 9
High Performance Packing & Aqueous Service Structured Packing page 10
Anti-Fouling Packing page 11
Column Internals page 12
Random Packing page 17
Worldwide Locations page 24
Contents
3. GTCTechnology
page 1
Engineered to Innovate®
GTC provides
complete vessel
fabrication
including tower
internals, field
erection and
installation of
entire distillation
columns.
Engineered to Innovate
GTC Technology is a global licensor of process technologies and mass transfer
solutions with the core mission of creating value for our clients. Refining,
petrochemical and chemical companies around the world rely on our advanced
technology to optimize production capacity and efficiency. We combine
unparalleled technical expertise and innovative thinking to solve complex
processing problems. GTC has earned a reputation of excellence by designing and
delivering high quality, strategic solutions for clients worldwide.
Providing Mass Transfer Solutions that Optimize Efficiency
GTC Technology’s Process Equipment Technology (PET) team designs and
provides specialized process equipment technology solutions that cover a broad
spectrum of conventional and proprietary trays, packing and other tower internals.
Beyond providing innovative process equipment, we offer practical solutions
backed by process optimization and energy saving studies.
At GTC, we recognize that no two situations or clients are alike. We pride ourselves
on working with each client to understand their business objectives and concerns,
combining the right mix of PET solutions to sustain their competitive position in
the marketplace.
GTC’s diverse portfolio offers the greatest potential to serve clients. We customize
our engineering and design equipment and services based on each client’s needs,
application and market. Our products and services include:
• Feasibility studies for column revamps
• Basic engineering package
• CFD modeling capabilities
• Equipment engineering, design, fabrication and delivery
• Project management and execution
• Equipment installation by GTC; at plant-site or vessel shop
• Installation site services supervision
• Start-up assistance
• Packed column internals
• Urgent replacement service
4. GTCTechnology
page 2
Engineered to Innovate®
Why GTC Technology?
Our engineers at GTC Technology know that high quality
equipment, advanced technology and on-time delivery are
critical to the success of your operation. We are committed
to our clients and hold ourselves accountable by delivering
products that optimize efficiency and lower costs through
energy saving equipment, innovative engineering, in-depth
analysis and reliable service. Drawing on our many years
of experience installing licensed technology around the
world, we have unparalleled technical expertise to design
and implement custom solutions for clients. As an ISO-9001 certified full-service
provider of mass transfer solutions, clients depend on GTC for fast on-time
delivery for urgent replacement needs.
Uniquely Positioned to Meet the Global Demands of the Industry
GTC Technology’s expansive capabilities allow us to mobilize resources to serve
a global clientele. With tight linkages between manufacturing and design, we can
respond quickly to regional demands with manufacturing and engineering facilities
located in the U.S., Korea, China, Singapore, Russia, Czech Republic and Mexico,
as well as sales agents stationed around the globe.
Our recent PET projects include providing engineering services, troubleshooting,
column revamp solutions for capacity and efficiency improvements, fast track
replacement services and turnkey installation packages for high-profile clients
worldwide.
Indoor liquid distributor flow testing
at GTC’s facility.
5. GTCTechnology
page 3
Engineered to Innovate®
Structured Packing
GTC Technology’s structured packing is designed to help clients achieve higher
capacity, higher efficiency and lower pressure drop. When selecting structured
packing, we advise our clients to consider several parameters that influence the
performance of the equipment including crimp height, crimp inclination angle,
element height, surface treatment, fouling tendency, system properties and service.
Our corrugated sheet structured packing, the industry standard clients have come
to expect, can be modified through the packing geometry, surface treatment
and manipulation of variables in order to increase efficiency and capacity. GTC
Technology’s extensive line of structured packing currently includes:
• GT-PAKTM
- Industry Standard Corrugated Sheet Packing
• GT-OPTIMTM
PAK High Capacity Structured Packing
• GT-OPTIM-eTM
PAK High Performance Packing
• GT-AQUATM
PAK Aqueous Service Structured Packing
• GT-GRIDTM
- Industry Standard Latice-Grating Packing
• GT-MixGRIDTM
- Industry Standard Corrugated Sheet Packing
GTCTechnology completed one of the largest structured packing installations in
the world with a tower diameter in excess of 15 meters.
6. GTCTechnology
page 4
Engineered to Innovate®
In this graph, the
overall performance
comparison shows an
inherent capacity
advantage for
structured packing
over random packing
at any chosen
efficiency basis.
Comparing Efficiency and Capacity of
Structured and Improved Random Packing
GTC often recommends structured packing over improved random packing.
When comparing relative capacity and efficiency for structured and improved
random packing, several conclusions can be drawn. First, notice that in the graph
above, capacity is an inverse relationship to efficiency. As capacity increases,
efficiency decreases. In addition, it is evident that as the specific surface area (SSA)
increases, structured packing displays greater efficiency.
The inherent advantage to structured packing is in utilizing the corrugated sheet
surface area while allowing higher vapor-liquid handling capacity in low pressure
or vacuum systems. The graph above confirms that structured packing can help
achieve much greater capacity compared to random packing at similar efficiencies
in low pressure systems.
Notes:
1. Random packing may achieve the same height equivalent to a theoretical stage (HETP) as
structured packing in some cases, but random packing would have lower capacity at these same
operating conditions.
2. Random packing has shown superior performance over structured packing in some systems,
such as high pressure (above 6 bar or 90 psia) services.
3. Refer to the additional graphs in this brochure for more complete comparison views.
Performance Comparison of
Structured Packing vs Random Packing
800
500
400
300
200
100
50
5 10 20 30 40 50 100
IncreasingEfficiency
SurfaceArea,SSA(m2/m3)
Increasing Capacity
Relative Capacity
Improved Rand
om
Packing
Structured
Packing
7. GTCTechnology
page 5
Engineered to Innovate®
This graph compares
Specific Surface
Area (SSA) to
Height Equivalent
to a Theoretical
Stage (HETP),
for GT-PAK.
As indicated,
when surface
area increases,
efficiency rises.
Comparing Surface Area and Efficiency of Structured Packing
Clients can estimate bed height by calculating the number of theoretical stages
required for the desired separation. The calculation can be carried out by
multiplying the expected HETP result for the selected structured packing. For
instance, GT-PAK 250Y has an HETP value of approximately 380 mm, the bed
height required per theoretical stage of separation for a typical low-alpha relative
volatility test system. For design applications, a minimum of 10 percent safety
margin would be applied to allow for changes in actual feed composition and
operating control variations. Therefore, an applied HETP of 420 mm is assumed.
For 20 stages, the design bed height would be 8.4 meters. For 60 stages, three beds
8.4 meters each in height would be required, keeping in mind that feed locations
may affect the actual bed arrangements.
Note:
Several factors that may reduce the efficiency of the structured packing, can impact the separation
and require more than the recommended 10 percent safety factor including:
• Aqueous or water-organic separations
• Two liquid phases
• “High-alpha” relative volatilities
• High pressure systems, above 6 bar (90 psia)
• Low liquid-to-vapor ratio
• Deep beds (over 20 theoretical stages)
• Foaming systems
• Scale-up from small diameter pilot columns
• Liquid or vapor mal-distribution
• Drip point density
Performance of Conventional
Structured Packing
800
500
400
300
200
100
50
100 200 400 600 800
15
30
61
91
122
152
244
63.039.431.523.615.77.9
Inches/
Theoretical Stage =
NOTES:
1. Typical“Low-Alpha”Hydrocarbon System shown.
2. HETP Values are System Dependent.
Design Safety Factors must be added.
SI Units
US Units
SSA(ft2
/ft3
)
1000 1600
IncreasingSurfaceArea
SurfaceArea,SSA(m2/m3)
Increasing Efficiency
Approximate HETP, mm/Theoretical Stage
GT-PAK TM
8. GTCTechnology
page 6
Engineered to Innovate®
Clients can
minimize energy
use while improving
product yield by
revamping process
towers with GTC
structured packing.
Comparing Pressure Drop and Capacity
of Structured and Random Packing
The relationship between pressure drop and capacity of structured and random
packing can be observed in the graph above. When conventional 250 m2
/m3
corrugated sheet structured packing is compared to #50 third-generation random
packing, structured packing has a greater capacity while maintaining a lower
pressure drop. When clients are looking to reduce energy costs and improve
column efficiency, GTC recommends revamping existing packed and trayed
columns with structured packing.
As displayed in the graph above, the random packing pressure drop is 15-20
percent higher than structured packing at the same column diameter and
throughput. Clients can benefit from structured packing by revamping existing
towers, reducing new column cross sectional area by 15-20 percent, improving
product purities and minimizing operating costs.
Performance Comparison
Structured Packing vs Random Packing
20
10
5
3
2
1
0.5
0.3
0.2
0.1
0.05
0.02 0.04 0.06 0.08 0.1
0.20
0.12
0.08
0.04
0.02
0.40
0.80
1.20
2.0
4.0
8.0
0.33 0.360.260.200.130.066 Cs [ft/s] =
NOTES:
1. Typical“Low-Alpha”Hydrocarbon System shown.
2. HETP Values are System Dependent.
Design Safety Factors must be added.
SI Units
US Units
InchesWC/Theoreticalstage
0.11
IncreasingPressureDrop
mbar/Theoreticalstage
Increasing Capacity
Capacity Factor, CS [m/s]
Random Rings #50 3rd Generation
Structured Pack 250Y
Conventi
onal
9. GTCTechnology
page 7
Engineered to Innovate®
Utilize this
graph to quickly
estimate minimum
bed heights and
minimum column
diameter for two
common packing
types in refinery
applications.
Estimations can
be based on typical
simulation results
for quantity of
theoretical stages
and internal flow
rates required
to meet the
specified product
compositions.
Comparing Efficiency and Capacity
of Structured and Random Packing
When comparing the efficiency and capacity of structured packing to random
packing, structured packing has significantly better performance.
There is a significant difference between the performance of GT-PAK 250Y
corrugated sheet structured packing and #50 third-generation random packing.
GT-PAK 250Y requires 50 percent less bed height for the same separation in
sizing new columns and can maintain greater capacity compared to random
rings. For revamped columns bed heights can be maintained, while a larger crimp
size structured packing can gain up to 50 percent greater capacity and yield the
same product purities as the #50 third-generation random packing. In addition,
clients can gain 10 percent more through-put, with better product purities at the
same column diameter or smaller by using GT-PAK 250Y as opposed to third-
generation random packing.
Notes:
1. The data represents a typical refinery application at atmospheric pressure.
2. A 10 percent minimum safety factor of added bed height is recommended to allow for feed
composition and operating control variations.
3. It is typical for new column sizing to be conservatively estimated at about 75 percent flood to
allow for future increases at efficient operation.
4. An 85 percent flood is considered a maximum safe design for revamp projects.
5. The maximum efficient column operation is around 90 percent flood for most modern packing.
Performance Comparison
Structured Packing vs Random Packing
1200
1000
800
600
400
200
0
0 .05 1 1.5 2.52
47.2
39.4
31.5
23.6
15.7
7.9
1.23 1.64 2.05 2.460.820.41Fs [ft/s] =
NOTES:
1. Typical Refinery Application, Atmospheric Pressure
2. HETP Values are System Dependent.
Design Safety Factors must be added.
SI Units
US Units
InchesWC/Theoreticalstage
3
HETP,mm
HeightEquivalenttoTheoreticalstage
Increasing Capacity
Vapor Rate: F-Factor, Fs = V5
*Dv0.5
[m/s]
HETP,Inches
RandomRings#503rdGeneration
StructuredPack250YConventional
10. GTCTechnology
page 8
Engineered to Innovate®
GT-PAK is
designed to
simplify equipment
installation
complexity,
reducing risk
while saving
clients costly
downtime during
unit shutdown.
GT-PAK™: Structured Packing
For direct replacement of industry standard conventional structured packing, GTC
offers GT-PAK. Our high efficiency structured packing is designed to achieve
maximum efficiency in column revamps or grassroots units and is available in
perforated, textured or corrugated sheet metal and can be customized for all major
surface area requirements. To simplify installation, the corrugated sheets that make
up our structured packing modules are assembled with screws, and periphery
column wall wiper banding is attached prior to shipment. These enhancements
ensure a stronger, more robust structured packing module that is easier to handle in
the field during installation. Additional GT-PAK features include:
• Excellent wetability with continually renewed mass transfer surface area
• Complete mixing of vapor and liquid with optimum radial distribution
• Waffled, grooved, lanced and dimpled texturing
• Standard 45° (Y) and 60° (X) crimp inclination
• Individual corrugated sheets forming intersecting channels
• Stronger module sections designed to resist damage during installation
PackingType
Nominal
Inclination
Angleº
Nominal
Specific Surface
Area (m2
/m3
)
Bulk
Density
(kg/m3
)
GT-PAKTM
750Y/X 45/60 750 260
GT-PAKTM
500Y/X 45/60 500 177
GT-PAKTM
440Y/X 45/60 440 168
GT-PAKTM
350Y/X 45/60 350 129
GT-PAKTM
300Y/X 45/60 300 161
GT-PAKTM
250Y/X 45/60 250 93
GT-PAKTM
220Y/X 45/60 220 80
GT-PAKTM
170Y/X 45/60 170 82
GT-PAKTM
150Y/X 45/60 150 79
GT-PAKTM
125Y/X 45/60 125 76
GT-PAKTM
80Y/X 45/60 80 58
GT-PAKTM
60Y/X 45/60 60 43
11. GTCTechnology
page 9
Engineered to Innovate®
GT-OPTIM PAK
can be used
in a wide range
of application
settings and
is designed to
optimize film
flow vapor-
liquid mixing,
reduce pressure
drop, increase
capacity and
provide excellent
separation
efficiency.
GT-OPTIMTM
PAK: High Capacity Structured Packing
GTC Technology has developed GT-OPTIM PAK, a product line of high
performance structured packing that delivers greater column throughput at the
same efficiency as traditional structured packing. GT-OPTIM PAK can be used
in a wide range of application settings and is designed to optimize film flow
vapor-liquid mixing, reduce pressure drop, increase capacity and provide excellent
separation efficiency. Our GT-OPTIM PAK product line includes:
GT-OPTIM™ PAK 750Y Highest Efficiency
GT-OPTIM™ PAK 500Y
GT-OPTIM™ PAK 440Y
GT-OPTIM™ PAK 350Y
GT-OPTIM™ PAK 300Y
GT-OPTIM™ PAK 250Y
GT-OPTIM™ PAK 220Y Highest Capacity
Prior to selecting high capacity structured packing, GTC recommends clients with
vacuum separations systems such as styrene, o-p Xylenes, iC8
-Toluene, cis-tran
Decalin, ChloroBenzene-EB and Cyclohexanone-Cyclohexanol to carefully
evaluate pressure drop and efficiency parameters.
Systems with close boiling components, such as styrene purification, require low
pressure drop distillation to avoid operational problems due to polymer formation.
Reduction in column pressure drop to the lowest drag possible is significant in
reducing bottoms reboiler temperatures, which naturally reduces polymerization
within the structured packing. The effect on relative volatility of low pressure
drop devices can also result in energy savings, specifically close boilers at vacuum
pressures.
GT-OPTIM PAK has a streamlined vapor profile at each layer interface, along with
a surface texture that optimizes the film-flow efficiency. This profile reduces liquid
holdup, which allows for greater capacity. Many other vacuum distillations show
significant energy savings and higher product purities with the lower pressure drop
of high performance structured packing.
12. GTCTechnology
page 10
Engineered to Innovate®
GT-OPTIM-eTM
PAK: High Performance Large Crimp Structured Packing
With the rising need from plant operators to increase product yield, improve
product purity specifications and reduce energy costs, GTC has developed
GT-OPTIM-e PAK to boost performance of refinery distillation units.
We work with each client to evaluate their separation system capacity, pressure
drop and efficiency parameters to determine what type of structured packing offers
the best solution for refining upgrades. In Fluidized Catalytic Cracking (FCC)
main fractionator revamps, our large crimp/low surface area structured packing
can increase the FCC converter effluent charge rates, enhance cracked naphtha
recovery from the light cycle oil and increase unit capacity by allowing a higher
suction pressure of the existing wet gas compressor.
For vacuum tower revamps, GT-OPTIM-e PAK is proven to increase vacuum gas
oil (VGO) lift from the vacuum residue (VR) and in distillation unit revamps,
our structured packing has been shown to improve cut-point sharpness along with
capacity increase.
GT-AQUATM
PAK: Aqueous Service Structured Packing
Aqueous-organic systems that utilize structured packing often result in lower
efficiency compared to typical hydrocarbon systems. The reduced performance
in aqueous systems can be attributed to surface tension effects and the resistance
of droplet beads spreading into the liquid film phase. In such conditions, proper
mixing with the vapor transport phase, product purification and separation cannot
be achieved.
GTC has designed GT-AQUA PAK, a product line of structured packing that
optimizes the spreading turbulence required for high efficiency within an aqueous
system. GTC recommends textured packing surfaces rather than smooth packing
surfaces because textured packing surfaces can achieve higher efficiency in high
surface tension systems. We work closely with clients to evaluate design separation
efficiencies prior to making a selection of packing for acetic acid-water, acrylonitrile-
water, acetone-water, alcohols-water, ethylene glycol and water-DMF systems.
GT-OPTIM-e PAK
combines the
advantages of
increased charge
rates, lower
pressure drops
and reduced energy
requirements to
create a higher
capacity and
efficiency
packing compared
to conventional
trays.
13. GTCTechnology
page 11
Engineered to Innovate®
GT-GRIDTM
and GT-MixGRIDTM
: Anti-Fouling Packing
GTC Technology has developed a product line of grid anti-fouling packing
designed to remove heavy metals, Con-carbons and residue entrainment in crude
atmospheric and vacuum distillation column wash sections.
Our GT-GRID and GT-MixGRID are suited for heat transfer sections such
as a slurry pumparound section of a FCC main fractionator. The anti-fouling
packing is designed to address high-temperature severe conditions that have coking
or polymerizing sediment. When clients require high throughput and fouling
resistance, GTC’s grids combined with the appropriate distributor are the best
solution for delivering industry leading performance.
GT-GRID and GT-MixGRID allow clients to achieve the highest capacity at the
lowest pressure drop, with minimum liquid holdup. Our anti-fouling packing
has been developed to withstand extreme operating conditions ranging from high
temperatures to high fluid velocities, without causing disruption due to pressure
surges. Benefits of our GT-GRID Classic Grating, Style A packing include:
• High-open area and low liquid hold up
• Resistance to plugging, coking and fouling
• Excellent heat transfer efficiency
• Highest capacity
• Excellent turndown ratio
• Wide operational flexibility
• Grid-bar packing, installed as sectional modules
• Structurally robust equipment designed to resist operational surges
• CS, 410, 304, 316L, Titanium, Monel, Duplex and other exotic alloys are
available upon request
We manufacture
a variety of
grids ranging
from traditional
bar-grating
lattice-type
grids (GT-GRID)
to corrugated
sheet structured
packing style
grids (GT-MixGRID).
Pictured above is GTC’s anti-fouling
packing; GT-GRID 20.
14. GTCTechnology
page 12
Engineered to Innovate®
GTC can upgrade
any internals that
require heavy-duty
mechanical design
in flashing-feed
systems.
GT-GRIDTM
and GT-MixGRIDTM
: Anti-Fouling Packing
PackingType Description Specific Surface Area (m2
/m3
)
GT-GRIDTM
20 Saw-tooth 45
GT-GRIDTM
30 Louvers 45
Benefits of our GT-MixGRID Corrugated Sheet, Style B packing include:
• Higher efficiency and de-entrainment than classic grid due to structured packing
configuration
• An “anti-fouling” smooth surface
• An alternating arrangement of individual corrugated sheets forming intersecting
channels for best in-bed mixing
• Corrugated sheets that are bolted for easy disassembly and cleaning, which
reduces replacement costs
PackingType Specific Surface Area (m2
/m3
)
GT-MixGRIDTM
80 X/Y 80
GT-MixGRIDTM
60 X/Y 60
GT-MixGRIDTM
40 X/Y 40
Column Internals
The importance of column internal design is often overlooked in packed columns.
GTC’s products are designed to improve the column operating performance
while maximizing the value of the plant investment. We offer a wide range of
GT-SMARTTM
column internals, including liquid/vapor distributors, collector
trays, packing supports, and retaining devices to help clients achieve high volume
throughput in new or existing towers.
15. GTCTechnology
page 13
Engineered to Innovate®
High Performance Liquid Distributors
Vapor and liquid distribution are of critical importance in ensuring
optimum performance is achieved in packed columns. GTC’s
Liquid Distributor product line is designed to reach high-quality
initial liquid dispersion in packed columns. Our engineers work
with clients to help them evaluate and select the best option of
system distributors for their process. We offer trough, pan, pipe or
spray type liquid distributors that can be constructed from standard
or exotic materials with optimum distribution configuration to
maximize column coverage and turndown.
Trough Type Distributors - High Performance
Model Type Description Features Benefits
TB-777 BaffleTrough
Distributor
Parting box and contoured trough
with side orifice liquid distribution
system: using deflector baffles
Liquid spreading diffuser plates
Contoured trough bottom
profile
Field leveling system
Drip point multiplying effect
allows larger orifices
Anti-fouling capability
Maximum operating range
Minimizes pressure drop across
troughs
Best coefficient of variation for
liquid distribution
TT-767 DripTrough Parting box and contoured trough
with side orifice liquid distribution
system: using triangular tubes
Drip tubes
Contoured trough bottom
profile
Field leveling system
Delivers discrete drip point
liquid
Anti-fouling capability
Maximum operating range
Minimizes pressure drop across
troughs
Best coefficient of variation for
liquid distribution
GTC’s trough type distributors achieve optimum
performance in packed columns and are the preferred
choice in the industry. Pictured above is GTC’s trough
type distributor modelTT-767.
16. GTCTechnology
page 14
Engineered to Innovate®
Tray/Deck/Pan Type Distributors - High Performance
GTC’s high performance deck-orifice type liquid distributors use narrow risers to
achieve the optimum orifice pattern for best distribution quality.
Model Type Description Features Benefits
HD-447 DeckType
Liquid
Distributor
Deck distributor with vapor risers
and liquid distribution orifices
Ring supported
Deck orifices
Narrow rectangular risers
With or without hats
Good turndown
Optimized vapor/liquid
distribution configuration
Re-distributor configuration
available
HD-437 DeckType
Liquid
Distributor
Deck distributor with vapor risers
and liquid distribution tubes
Ring supported
Orifices are elevated in drip
tubes
Narrow rectangular risers
With or without hats
Maximum turndown
Fouling resistance
Optimized vapor/liquid
distribution configuration
Re-distributor configuration
available
SD-346RM PanType Liquid
Distributor
(bucket)
Pan distributor with vapor risers
and liquid distribution orifices
Clip supported or between body
flanges
Used in columns < 30’’diameter
Designed as a single piece or
two halves
Orifices in pan or drip tubes
Optimized vapor/liquid
distribution configuration
Re-distributor configuration
available
Good turndown
Pictured above is GTC’s deck type liquid distributor;
model HD-447.
17. GTCTechnology
page 15
Engineered to Innovate®
Feed Distributor Devices
Feed distribution is a critical component to achieving desired column performance.
Flashing feed distribution is especially important for controlling phase separation,
momentum and direction of the fluids. GTC offers a range of liquid/vapor hooded
pipes, perforated pipes, vee-baffles and vapor horns built from carbon and alloy
steel, designed to optimize tower performance. Our liquid feed piping features
precisely sized openings and orifices for proper distribution, various configurations
to deliver liquid to the optimum device zone and flanged spool designs for ease
of assembly and disassembly. Our flashing feed distributors offer segmented plate
designs and heavy duty designs that can withstand high inlet forces.
Model Type Description Features Benefits
GT-OPTIMFLOWTM
RadialType
Distributor
A custom designed annular
2-phase feed horn
Tangential or radial nozzles
De-entrainment vanes
Excellent phase separation
Low pressure drop
Good phase distribution
VEB-661 Vee-Baffle
Distributor
Heavy duty 2-phase feed
impingement baffle with wear
plate
V-shape impingement plate
design
Tee-box exit configuration
Absorbs 2-phase feed kinetic
energy
Directs flow patterns and
initiates vapor liquid separation
Reduces entrance velocities
FPS Feed Pipe Straight feed pipe with orifices
or tubes
Straight pipe configuration Provides quality distribution of
liquid and vapor
FPT Feed Pipe “T”shaped feed pipe with orifices
or tubes
T- pipe configuration Provides quality distribution of
liquid and vapor
FPH Feed Pipe “H”shaped feed pipe with orifices
or tubes
H- pipe configuration Provides quality distribution of
liquid and vapor
FPL Feed Pipe Feed pipe with multiple laterals
with orifices or tubes
Multi-lateral pipe
configuration
Provides quality distribution of
liquid and vapor
Pipe Type Liquid Distributors
Model Type Description Features Benefits
SND-900 Spray Nozzle
Distributor
Pipe with laterals and spray
nozzle distributor (standard)
Various spray nozzle patterns
Header/lateral pipe
configuration
Uniform distribution
Pressurized flow stream
Minimum residence time
*SND-950 available for anti-fouling capability
GTC offers a vee-baffle distributor;
modelVEB-661.
18. GTCTechnology
page 16
Engineered to Innovate®
Packing Supports
Model Type Description Features Benefits
PSG-101 Packing Support
Grid
Standard structured packing
support grid
Custom designed for application
Support beams included as
required
Minimal pressure drop
Designed for mechanical
integrity
ISB-201 Injection
Support Beam
Random packing support Gas injection design with
sinusoidal wave structure
Support beams included as
required
Minimal pressure drop
Designed for mechanical
integrity
GTC’s packing supports and hold-downs are designed to optimize the performance
of packed bed systems. We offer a full product line of packed beds, designed with
superior strength, mechanical integrity and the maximum open area achievable for
specified vapor and liquid passage.
Packing Hold-Downs
Model Type Description Features Benefits
HDB-110 Hold-Down Bar Hold-down bar for structured
packing
Simple design for small towers
95% open area
Functional design minimal
space requirements
Minimal pressure drop
Quick installation
HDG-111 Hold-Down Grid Structured packing hold-down
grid
Uplift resistant design Functional design with
minimal space requirements
Minimal pressure drop
Quick installation
HDG-112 Hold-Down Grid Random packing hold-down
grid sized for specific packing
diameter
Uplift resistant design Functional design with
minimal space requirements
Minimal pressure drop
Quick installation
19. GTCTechnology
page 17
Engineered to Innovate®
Liquid Collection Trays
Poor liquid collection tray design can significantly downgrade column
performance. GTC recommends that clients carefully evaluate liquid collection
trays to ensure proper product draw and liquid vapor distribution. GTC offers
an extensive line of collector/re-distributor products built from standard or exotic
materials featuring a variety of shapes and configurations. Fully seal-welded or
bolted designs are available for applications of total draw-off to various downcomer
and overflow designs.
Model Type Description Features Benefits
CLT-601 CollectorTray Collection/redistribution tray
with optional downcomers
and liquid draw-off
arrangements
Custom designed for application
Vapor risers
Beams provided as required for
mechanical integrity
Optimum riser configuration
CVT-621 Vane type
collection/
redistribution
tray
Liquid vane collector tray
with radial ring channel and
optional downcomers and
liquid draw-off arrangements
Integral hat/vane collector
Channel collector troughs
Low pressure drop
Random Packing
Packed towers were first introduced in the 1900s with Raschig Rings and Ceramic
Saddles utilized in distillation columns. By the end of the 1950s, random packing
became the most widely used packing in the petrochemical, chemical and refining
industries. Over time, random packing designs evolved and a second-generation
of a Pall-type slotted ring was commercialized. The second-generation of rings
permitted liquid flow through the element walls and were equal in height and
diameter with a 1:1 aspect ratio.
In the 1980s, a third-generation of rings introduced further improvements to
slotted rings and could achieve even higher efficiency and capacity. This hybrid of
improved geometrical shapes is focused on an optimum orientation by redesigning
as a lower height aspect ratio in a range of 1:2 to 1:3.
1st generation Raschig rings, saddles 1:1 aspect ratio as solid surface
2nd generation Pall ring or GT-PRTM
ring 1:1 aspect ratio with surface utilization
3rd generation GT-IRTM
& GT-CRTM
rings 1:2 to 1:3 aspect ratio for orientation
20. GTCTechnology
page 18
Engineered to Innovate®
Random Packing
GTC offers all commercial sizes and shapes of each generation of rings in metallic,
non-metallic, carbon and alloy steel materials. Although today it is more common
to use structured packing in packed columns, there are circumstances in which
random packing can provide better performance and throughput capacity. For
instance, in certain high pressure and foaming service systems, our random packing
can achieve superior performance compared to structured packing.
We recommend our random packing for high pressure gas absorption systems,
cryogenic Demethanizers, and other high pressure and/or high liquid rate systems
where trays or structured packing are not the preferred choice. Our GT-CR and
GT-IR rings are well-suited to handle very high liquid applications, in particular
where foaming is a concern. The geometric packing shapes have been developed
to minimize foam while allowing greater liquid and vapor loads than older
generations of packing.
Basic Design Criteria
The performance of GTC’s random packing depends on the geometric shape
and size. The dimensional parameters define both the “Packing Factor” (Fp)
and “Specific Surface Area” (SSA). For our packing, a lower packing factor is
synonymous with a lower pressure drop, resulting in higher capacity. The total
effective surface area inside our random packing shapes define the efficiency, with
higher surface areas producing higher efficiencies.
The capacity of our random packing is a function of its packing factor (Fp). A
good approximation of the difference in capacity between two types of our packing
materials can be calculated by the square root of their packing factor ratio.
Our small size packings (with bigger Fp & SSA) generate greater efficiency
resulting in shorter bed height. Our large size packings (with lesser Fp & SSA) have
a larger open area and allow for greater column throughput (vapor–liquid handling
capacity). The capacity criteria for our standard design is flooding < 70-85 percent
and pressure drop < 4 mbar/m-bed (0.5 inch H2
O/ft-bed).
GTC offers all
commercial sizes
and shapes of each
generation of rings
in metallic, non-
metallic, carbon
and alloy steel
materials.
21. GTCTechnology
page 19
Engineered to Innovate®
Random Packing: GT-CRTM
Rings
GT-CRTM
Third Generation Metal Rings:
Model Void Fraction Specific Surface Area (m2
/m3
) Packing Factor
GT-CRTM
1.0 96.9 250 40
GT-CRTM
1.5 97.2 188 33
GT-CRTM
2.0 97.8 144 26
GT-CRTM
2.5 97.8 123 23
GT-CRTM
3.0 98.0 103 18
GT-CRTM
4.0 98.5 74 14
GT-CRTM
5.0 98.8 49 11
GT-CRTM
Third Generation Plastic Rings:
Model Void Fraction Specific Surface Area (m2
/m3
) Packing Factor
GT-CRTM
0A 89 320 55
GT-CRTM
1A 92 230 30
GT-CRTM
2A 93 140 18
GT-CRTM
2 94 118 15
GT-CRTM
3A 95 79 12
22. GTCTechnology
page 20
Engineered to Innovate®
Pressure Drop Data for GT-CRTM
Third Generation Rings
C-Factor: CS (m/sec)
GT-CRTM
1.0 Pressure Drop
0.10
200 2.40
100
80
60
40
20
1.20
10
8
6
4
3
0.02 0.04 0.06 0.08 0.10 0.20
0.12
0.165 0.33 0.66
C-Factor: CS (ft/sec)
SI Units
US Units
* Note: C-Factor, CS = Vapor Superficial Velocity
P,mmliquid/m
P,Inchesliquid/ft
ρV
ρL- ρv
x
Dry P
5 m3/hr/m2 (2 gpm/ft2)
12 m3/hr/m2 (5 gpm/ft2)
25 m3/hr/m2 (10 gpm/ft2)
50 m3/hr/m2 (20 gpm/ft2)
75 m3/hr/m2 (30 gpm/ft2)
GT-CRTM
2.0 Pressure Drop
0.10
200 2.40
100
80
60
40
20
1.20
10
8
6
0.02 0.04 0.06 0.08 0.10 0.20
0.12
0.165 0.33 0.66
ρV
ρL- ρv
x
C-Factor: CS (m/sec)
C-Factor: CS (ft/sec)
SI Units
US Units
* Note: C-Factor, CS = Vapor Superficial Velocity
P,Inchesliquid/ft
ρV
ρL- ρv
x
P,mmliquid/m
12 m3/hr/m2 (5 gpm/ft2)
25 m3/hr/m2 (10 gpm/ft2)
75 m3/hr/m2 (30 gpm/ft2)
100 m3/hr/m2 (40 gpm/ft2)
125 m3/hr/m2 (50 gpm/ft2)
50 m3/hr/m2 (20 gpm/ft2)
Dry P
P,mmliquid/m
C-Factor: CS (m/sec)
GT-CRTM
1.5 Pressure Drop
0.10
200 2.40
100
80
60
40
20
1.20
10
8
6
4
3
0.02 0.04 0.06 0.08 0.10 0.20
0.12
0.165 0.33 0.66
C-Factor: CS (ft/sec)
P,Inchesliquid/ft
US Units
SI Units
* Note: C-Factor, CS = Vapor Superficial Velocity
ρV
ρL- ρv
x
5 m3/hr/m2 (2 gpm/ft2)
12 m3/hr/m2 (5 gpm/ft2)
50 m3/hr/m2 (20 gpm/ft2)
75 m3/hr/m2 (30 gpm/ft2)
100 m3/hr/m2 (40 gpm/ft2)
25 m3/hr/m2 (10 gpm/ft2) 125 m3/hr/m2 (50 gpm/ft2)
Dry P
GT-CRTM
2.5 Pressure Drop
0.10
200 2.40
100
80
60
40
20
1.20
10
8
6
4
0.02 0.04 0.06 0.08 0.10 0.20
0.12
0.165 0.33 0.66
C-Factor: CS (m/sec)
C-Factor: CS (ft/sec)
SI Units
US Units
* Note: C-Factor, CS = Vapor Superficial Velocity
P,Inchesliquid/ft
ρV
ρL- ρv
x
P,mmliquid/m
12 m3/hr/m2 (5 gpm/ft2)
25 m3/hr/m2 (10 gpm/ft2)
75 m3/hr/m2 (30 gpm/ft2)
100 m3/hr/m2 (40 gpm/ft2)
125 m3/hr/m2 (50 gpm/ft2)
50 m3/hr/m2 (20 gpm/ft2)
Dry P
23. GTCTechnology
page 21
Engineered to Innovate®
Pressure Drop Data for GT-CRTM
Third Generation Rings
GT-CRTM
3.0 Pressure Drop
0.10
200 2.40
100
80
60
40
20
1.20
10
8
6
0.02 0.04 0.06 0.08 0.10 0.20
0.12
0.165 0.33 0.66
C-Factor: CS (m/sec)
C-Factor: CS (ft/sec)
US Units
* Note: C-Factor, CS = Vapor Superficial Velocity
P,Inchesliquid/ft
ρV
ρL- ρv
x
SI Units
P,mmliquid/m
12 m3/hr/m2 (5 gpm/ft2)
25 m3/hr/m2 (10 gpm/ft2)
75 m3/hr/m2 (30 gpm/ft2)
100 m3/hr/m2 (40 gpm/ft2)
125 m3/hr/m2 (50 gpm/ft2)
50 m3/hr/m2 (20 gpm/ft2)
Dry P
GT-CRTM
5.0 Pressure Drop
0.10
200 2.40
100
80
60
40
20
1.20
10
8
6
4
2
0.02 0.04 0.06 0.08 0.10 0.20
0.12
0.165 0.33 0.66
C-Factor: CS (m/sec)
C-Factor: CS (ft/sec)
US Units
* Note: C-Factor, CS = Vapor Superficial Velocity
P,Inchesliquid/ft
ρV
ρL- ρv
x
SI Units
P,mmliquid/m
12 m3/hr/m2 (5 gpm/ft2)
25 m3/hr/m2 (10 gpm/ft2)
75 m3/hr/m2 (30 gpm/ft2)
100 m3/hr/m2 (40 gpm/ft2)
125 m3/hr/m2 (50 gpm/ft2)
50 m3/hr/m2 (20 gpm/ft2)
Dry P
GT-CRTM
4.0 Pressure Drop
0.10
200 2.40
100
80
60
40
20
1.20
10
8
6
4
0.02 0.04 0.06 0.08 0.10 0.20
0.12
0.165 0.33 0.66
C-Factor: CS (m/sec)
C-Factor: CS (ft/sec)
US Units
* Note: C-Factor, CS = Vapor Superficial Velocity
P,Inchesliquid/ft
ρV
ρL- ρv
x
SI Units
P,mmliquid/m
12 m3/hr/m2 (5 gpm/ft2)
25 m3/hr/m2 (10 gpm/ft2)
75 m3/hr/m2 (30 gpm/ft2)
100 m3/hr/m2 (40 gpm/ft2)
125 m3/hr/m2 (50 gpm/ft2)
50 m3/hr/m2 (20 gpm/ft2)
Dry P
24. GTCTechnology
page 22
Engineered to Innovate®
Random Packing: GT-PRTM
and GT-IRTM
Rings
GT-PRTM
Second Generation Metal Rings:
Model Void Fraction Specific Surface Area (m2
/m3
) Packing Factor
GT-PRTM
16 93.3 344 81
GT-PRTM
25 95.9 202 56
GT-PRTM
38 97.4 142 40
GT-PRTM
50 97.5 98 27
GT-PRTM
90 98.3 57 18
GT-PRTM
Second Generation Plastic Rings:
Model Void Fraction Specific Surface Area (m2
/m3
) Packing Factor
GT-PRTM
16 86 354 97
GT-PRTM
25 90 207 52
GT-PRTM
38 91 128 32
GT-PRTM
50 92 102 25
GT-PRTM
90 93 72 16
GT-IRTM
Third Generation Metal Rings:
Model Void Fraction Specific Surface Area (m2
/m3
) Packing Factor
GT-IRTM
15 96.4 282 51
GT-IRTM
25 97.2 225 41
GT-IRTM
40 98.1 152 24
GT-IRTM
50 98.1 102 18
GT-IRTM
70 98.3 60 12
25. GTCTechnology
page 23
Engineered to Innovate®
Pressure Drop Data for GT-PRTM
Second Generation Rings
C-Factor: CS (m/sec)
GT-PRTM
25 Pressure Drop
0.1
200 2.40
100
80
60
40
20
10
1.20
8
7
0.03 0.04 0.06 0.08 0.10 0.20
0.12
0.165 0.33 0.66
C-Factor: CS (ft/sec)
US Units
* Note: C-Factor, CS = Vapor Superficial Velocity
P,Inchesliquid/ft
ρV
ρL- ρv
x
SI Units
P,mmliquid/m
5.0 m3/hr/m2 (2 gpm/ft2)
12.5 m3/hr/m2 (5 gpm/ft2)
50 m3/hr/m2 (20 gpm/ft2)
75 m3/hr/m2 (30 gpm/ft2)
100 m3/hr/m2 (40 gpm/ft2)
25 m3/hr/m2 (10 gpm/ft2)
Dry P
5.0 m3/hr/m2 (2 gpm/ft2)
12.5 m3/hr/m2 (5 gpm/ft2)
50 m3/hr/m2 (20 gpm/ft2)
75 m3/hr/m2 (30 gpm/ft2)
100 m3/hr/m2 (40 gpm/ft2)
25 m3/hr/m2 (10 gpm/ft2)
Dry P
2.5 m3/h/m2 (1 gpm/ft2)
5.0 m3/h/m2 (2 gpm/ft2)
25 m3/h/m2 (10 gpm/ft2)
50 m3/h/m2 (20 gpm/ft2)
100 m3/h/m2 (40 gpm/ft2)
12.5 m3/h/m2 (5 gpm/ft2)
GT-PRTM
50 Pressure Drop
0.10
200 2.40
100
80
60
40
20
10
1.20
8
6
4
3
0.040.03 0.06 0.08 0.10 0.20
0.12
0.165 0.33 0.66
C-Factor: CS (m/sec)
C-Factor: CS (ft/sec)
US Units
* Note: C-Factor, CS = Vapor Superficial Velocity
P,Inchesliquid/ft
ρV
ρL- ρv
x
SI Units
Dry P
P,mmliquid/m
GT-PRTM
38 Pressure Drop
0.10
200 2.40
100
80
60
40
20
10
1.20
8
6
4
0.03 0.04 0.06 0.08 0.10 0.20
0.12
0.165 0.33 0.66
C-Factor: CS (m/sec)
C-Factor: CS (ft/sec)
US Units
* Note: C-Factor, CS = Vapor Superficial Velocity
P,Inchesliquid/ft
ρV
ρL- ρv
x
SI Units
P,mmliquid/m
5.0 m3/h/m2 (2 gpm/ft2)
12.5 m3/h/m2 (5 gpm/ft2)
25 m3/h/m2 (10 gpm/ft2)
50 m3/h/m2 (20 gpm/ft2)
100 m3/h/m2 (40 gpm/ft2)
Dry P
2.5 m3/h/m2 (1 gpm/ft2)
5.0 m3/h/m2 (2 gpm/ft2)
25 m3/h/m2 (10 gpm/ft2)
50 m3/h/m2 (20 gpm/ft2)
100 m3/h/m2 (40 gpm/ft2)
12.5 m3/h/m2 (5 gpm/ft2)
Dry P
GT-PRTM
90 Pressure Drop
0.1
200 2.40
100
80
60
40
20
10
1.20
0.040.02 0.06 0.08 0.10 0.20
0.12
0.165 0.33 0.66
C-Factor: CS (m/sec)
C-Factor: CS (ft/sec)
US Units
* Note: C-Factor, CS = Vapor Superficial Velocity
P,Inchesliquid/ft
ρV
ρL- ρv
x
SI Units
P,mmliquid/m
26. GTCTechnology
page 24
Engineered to Innovate®
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