This document discusses different types of packing materials used in distillation columns, including trays and structured/random packings. It describes the main types of trays like sieve, bubble cap, and valve trays as well as common packing materials like Rasching rings, Intalox saddles, and Mellapak. The document compares traits of trays and packed columns and discusses how new high-speed and high-powered adaptive valve trays are modifications of conventional trays to improve efficiency. In conclusion, bubble cap trays are most commonly used in industry over sieve trays and packed columns have higher mass transfer area but also higher costs than tray columns.
A boiler or steam generator is a device used to create steam by applying heat energy to water. Although the definitions are somewhat flexible, it can be said that older steam generators were commonly termed boilers and worked at low to medium pressure.
In petroleum refining, the Crude Distillation Unit (CDU) (often referred to as the Atmospheric Distillation Unit) is usually the first processing equipment through which crude oil is fed. Once in the CDU, crude oil is distilled into various products, like naphtha, kerosene, and diesel, that then serve as feedstocks for all other processing units at the refinery.
A boiler or steam generator is a device used to create steam by applying heat energy to water. Although the definitions are somewhat flexible, it can be said that older steam generators were commonly termed boilers and worked at low to medium pressure.
In petroleum refining, the Crude Distillation Unit (CDU) (often referred to as the Atmospheric Distillation Unit) is usually the first processing equipment through which crude oil is fed. Once in the CDU, crude oil is distilled into various products, like naphtha, kerosene, and diesel, that then serve as feedstocks for all other processing units at the refinery.
Burner Design, Operation and Maintenance on Ammonia PlantsGerard B. Hawkins
Burner Design, Operation and Maintenance on Ammonia Plants
Brief History
Reformer Burner Types/Design
Types of Reformers
Combustion Characteristics
Excess Air/Heater Efficiency
Maintenance, Good Practice
Low Nox Equipment
Summary
In the plant, ammonia is produced from synthesis gas containing hydrogen and nitrogen in the ratio of approximately 3:1. Besides these components, the synthesis gas contains inert gases such as argon and methane to a limited extent. The source of H2 is demineralized water and the hydrocarbons in the natural gas. The source of N2 is the atmospheric air. The source of CO2 is the hydrocarbons in the natural gas feed. Product ammonia and CO2 is sent to urea plant. The present article intended the description of ammonia plant for natural gas based plants and the possible material balance of some section.
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
Look at two main types
Explain mechanisms
Explain prevention of cracking
Three main types
1 Carbon cracking
2 Boudouard carbon formation
3 CO reduction
(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
Distillation is the basic and oldest chemical separation process used in the chemical industries and petroleum refining.
Let's recognize the difference between Packed and Plate columns in industry and the comparison of their usage!
Steam Reforming - The Basics of reforming, shapes and carbon:
Steam Reforming Catalysis :
Chemical reactions
Catalyst shape design
Catalyst chemistry
Carbon formation and removal
The explosion hazard in urea process (1)Prem Baboo
In Urea plant passivation air is used in reactor, stripper and downstream of the all equipments. The reactor liner material used Titanium, Zirconium, SS 316L (urea grade), 2RE-69 and duplex material .except Titanium and Zirconium all stainless steel required more passivation air. In CO2 some quantity of Hydrogen is present about 0.14% to 0.2% . The passivation oxygen and Hydrogen makes explosive mixture. To avoid a fire or explosion in a process vessel is to introduce inert (noncombustible) gases in such a way that there is never a mixture with a combustible concentration in exit of MP vent. Mixtures of fuel, oxygen, and inert gases are not combustible over the entire range of composition. In CO2 stripping process the HP scrubber is the risky vessel and this vessel consisting blanketing sphere, Heat exchanger part and a scrubbing part. With help of triangular diagram that shows the shape of the combustible/noncombustible regions for a typical gaseous mixture of fuel, oxygen, and inert at specified temperature and pressure. Present article how to avoid that combustible rang and how to tackle that gases in CO2 & ammonia stripping process.
Burner Design, Operation and Maintenance on Ammonia PlantsGerard B. Hawkins
Burner Design, Operation and Maintenance on Ammonia Plants
Brief History
Reformer Burner Types/Design
Types of Reformers
Combustion Characteristics
Excess Air/Heater Efficiency
Maintenance, Good Practice
Low Nox Equipment
Summary
In the plant, ammonia is produced from synthesis gas containing hydrogen and nitrogen in the ratio of approximately 3:1. Besides these components, the synthesis gas contains inert gases such as argon and methane to a limited extent. The source of H2 is demineralized water and the hydrocarbons in the natural gas. The source of N2 is the atmospheric air. The source of CO2 is the hydrocarbons in the natural gas feed. Product ammonia and CO2 is sent to urea plant. The present article intended the description of ammonia plant for natural gas based plants and the possible material balance of some section.
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
Look at two main types
Explain mechanisms
Explain prevention of cracking
Three main types
1 Carbon cracking
2 Boudouard carbon formation
3 CO reduction
(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
Distillation is the basic and oldest chemical separation process used in the chemical industries and petroleum refining.
Let's recognize the difference between Packed and Plate columns in industry and the comparison of their usage!
Steam Reforming - The Basics of reforming, shapes and carbon:
Steam Reforming Catalysis :
Chemical reactions
Catalyst shape design
Catalyst chemistry
Carbon formation and removal
The explosion hazard in urea process (1)Prem Baboo
In Urea plant passivation air is used in reactor, stripper and downstream of the all equipments. The reactor liner material used Titanium, Zirconium, SS 316L (urea grade), 2RE-69 and duplex material .except Titanium and Zirconium all stainless steel required more passivation air. In CO2 some quantity of Hydrogen is present about 0.14% to 0.2% . The passivation oxygen and Hydrogen makes explosive mixture. To avoid a fire or explosion in a process vessel is to introduce inert (noncombustible) gases in such a way that there is never a mixture with a combustible concentration in exit of MP vent. Mixtures of fuel, oxygen, and inert gases are not combustible over the entire range of composition. In CO2 stripping process the HP scrubber is the risky vessel and this vessel consisting blanketing sphere, Heat exchanger part and a scrubbing part. With help of triangular diagram that shows the shape of the combustible/noncombustible regions for a typical gaseous mixture of fuel, oxygen, and inert at specified temperature and pressure. Present article how to avoid that combustible rang and how to tackle that gases in CO2 & ammonia stripping process.
Procedure for Steam Reforming Catalyst Reduction with LPG Feed
Scope
This procedure may be used for the reduction of VULCAN Series Catalysts for the general steam reforming of LPG.
It is strongly advised that this procedure is adopted only where there is no other option available to use hydrogen, a hydrogen-rich gas or natural gas for the reduction stage. Reduction using the cracking of heavier hydrocarbons carries an extreme risk of catastrophic carbon formation in the event of any error in execution of the procedure.
Introduction
LPG is not normally utilized for steam reforming catalyst reduction although it can be used successfully. Caution is required if heavier hydrocarbons are used for catalyst reduction. Although operators have been able to reduce catalysts by using heavier hydrocarbon cracking, this has only been adopted where no other reductant option is available. The risk of carbon formation greatly increases as the carbon number of the feed increases when the catalyst is in the unreduced state. For the purposes of this procedure, LPG may range from a hydrocarbon mixture which is predominantly propane to one which is predominantly butane.
SYNGAS CONDITIONING UNIT FEASIBILITY CASE STUDY: COAL-TO-LIQUIDSGerard B. Hawkins
SYNGAS CONDITIONING UNIT FEASIBILITY CASE STUDY: COAL-TO-LIQUIDS
Case Study: #0953616GB/H
HT SHIFT REACTOR CATALYST SPECIFICATION
Process Specification
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The Syngas Conditioning Unit is part of a proposed coal-to-liquids complex in which synthesis gas is produced by gasification of coal for downstream processing in a Fischer Tropsch reactor and Hydrocracker unit.
this ppt is made with the reference of heat exchangers that have been used in NHFI, it almost covers their every aspect that is their working, maintenance, and safety !!
so please suit yourself!!!
Rheological test can be very helpful tools for polymer processing and development. This presentation is designed to be an informative introduction and guide to rheological tests, and finding correlations between equipment and processing techniques.
Slides for the eLearning course Separation and purification processes in biorefineries (https://open-learn.xamk.fi) in IMPRESS project (https://www.spire2030.eu/impress).
Section: Distillation
Subject: 0.2 Introduction to distillation.
It is about the Versatility of Packed Column over Plate Column. It has all types of Plate or Tray column and Plane column. Condition favoring for the columns and also advantages and disadvantages.
pipe one of the main article that is used in our daily life.its being manufactured and used in industries in large scale. because of its large application and uses they are being manufactured in varies levels and types
Slides for the eLearning course Separation and purification processes in biorefineries (https://open-learn.xamk.fi) in IMPRESS project (https://www.spire2030.eu/impress).
Section: Mass transfer
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connected to the spacecraft moved from the boundaries of a coronal hole
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Professional air quality monitoring systems provide immediate, on-site data for analysis, compliance, and decision-making.
Monitor common gases, weather parameters, particulates.
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04
1. Department Of Chemical Engineering
Seminar On
• Presented By:-
Bande Dnyaneshwar Ramakant
• Roll :-04 Under the guidance of :-S.R.Yadav
PACKING IN DISTILLATION COLUMN
2. Content
• Introduction
• Selection of column type: Plate or Packed
• Types of packing material
• 1) Sieve Tray
• b)Bubble Cap Tray
• c)Valve Tray
• New Generation Tray
• Packed Column
• Packing Material
• Types of packing
• New Generation of Packing Material in Structural packing
3. Introduction
• Packing Column used in following unit process
1) Distillation
2) Liquid-liquid Extraction
3) Gas absorption
1)Distillation
• About distillation
• Principle
• Classification of distillation
4. Selection of column type: Tray & Packed
• Flow
• performance
• Pressure drop
• Suitable liquid
• Cleaning
• Corrosion problem
• Diameter of column
5. Types of packing material
• 1) Tray or plate column
1) Types of packing of Tray
• 2)Packed column
2) Types of packing material
Selection of tray
Capacity & efficiency
Pressure drop
Liquid flow
Turndown ratio
Cost
6. A) Tray
a) Sieve Tray
Construction of sieve tray(1.5-25mm)
Arrangement of holes
Flow pattern
Pressure drop
maintenance
Application
7. b)Bubble Cap Tray
Construction of bubble cap tray(20-160mm)
Arrangement of holes
Flow pattern
Pressure drop
maintenance
Application
8. c)Valve Tray
Construction of valve tray(40-150mm)
Arrangement of holes
Flow pattern-
Pressure drop-
Maintenance-
Application
11. • It is modification of valve tray
• It has more efficacy
• It has more contact area of liquid and gas
• Valve tray as one of the most important mass transfer and heat
transfer equipment's for vapor–liquid is widely used in distillation,
absorption and extraction units of petroleum, chemical industry
High-Powered Adaptive Valve
Tray
12. Comparison of Trays:
Tray
type
Capacity Efficacy Pressure
drop
Entrainment turndown cost
Bubble
cap Medium medium High
3times than
Sieve tray Excellent
100-
200%more
than sieve
tray
valve
High high Medium medium
4 to 10.1 20-50%
more than
sieve tray
sieve High high medium medium 2.1 Cheapest
for all type
13. Advantages of tray column
• Capacity, efficiency, pressure drop is more than packed column
• Cost is less than packed column
• Maintains easier than packed column
• High liquid residence time
15. Packing Material
Ceramic: superior wettability, corrosion resistance at elevated
1)Rasching rings, 2 ) intalox saddle 3) berl saddle,
Metal: superior strength & good wettability& good wettability
1)intalix 2)pall rings 3)super rings 4) top pack
Plastic: inexpensive, good strength but may have poor wettability at low
liquid rate
• e.g-1) High flow ring,2) super intalox saddle 3) plastic hasckett
19. Comparison of random &structure packing
Random packing
Structure
packingRasching ring and
saddle
Through flow
Relative cost low moderate high
Pressure drop moderate low high
efficiency moderate high Very high
Vapour capacity Fairly high high high
Typical turndown ratio 2 2 2
20. New Generation of Packing Material in
Structural packing
• Mellapak
• Optiflow
• Mellapak plus
Mellapak
Arrangement
Flow pattern
Application
Efficacy
21. Comparison of Tray and packed column
Tray
column
Packed column
Area required More Less
Pressure drop More Less
Maintains Easy Difficult
Mass transfer
area
Less More
22. Conclusion
• A bubble cap tray use to a in industry more than sieve tray, valve tray
• A packed column is more expensive than tray column
23. Reference
• Robert E. Treybal”,Mass Transfer operations", distillation, Gas absorption,
1992 p.275,342.
• Henry Z.Kister”,distillation design p 833,1980
• K. Hartmann, V. Kiselev (1998) New Highspeed Fractionation Trays For
Mass- Transfer Columns, AIChE Annual Meeting, Miami Beach, FL,
November 15-20, 1998, Session ”Advances in Distillation Hardware”,
Paper 134d