Sources of fatty amines
The natural reaction pathways of fatty amines
Manufacture of hetero-alkyl amines
tertiary amines
quaternary amine salts
Directional influence of H2, NH3 and H2O on:
amine distribution
conversion and reaction rate
Oleochemical Technology. Production of fatty acids & glycerine starting from vegetable & animal oil and fats Hydrolysis is the basic production step, the fats and oils are split into crude glycerine and a mixture of crude fatty acids, under the combined action of water, temperature and pressure. The temperature exceeds 200°C and the products are kept under pressure for more than 20 minutes.. Fats & oils crude glycerine + crude fatty acids + water
3. • A process for the esterification of a triglyceride. • The process comprises forming a single phase solution of said triglyceride in an alcohol selected from methanol and ethanol, the ratio of alcohol to triglyceride being 15:1 to 35:1. • The solution further comprises a co-solvent in an amount to effect formation the single phase and a base catalyst for the esterification reaction. • After a period of time, ester is recovered from the solution. • Esterification is rapid and proceeds essentially to completion. • The esters may be used as biofuel or biodiesel
4. Glycerine (also called glycerin or glycerol) is an alcohol which is used as a moisturizer in soaps and lotions. Glycerine has a sweet taste, and it can be used as a food preservative and a non-sugar sweetener.
5. Glycerine Lubricants (jet engine, refrigeration) Plasticizer for Polyvinyl Butyral (PVB) Explosives Polyurethane Foam
6. Examples of Derivative
7. Process involves 1. A fatty acid or fatty acid mixture is esterified in a column reactor. 4. As the liquid flows down the trays it encounters progressively drier lower alkanol. 5. The ester product recovered from the bottom of the reactor has an ester content of at least 99 mole % (calculated on a lower alkanol free basis). 2. Relatively dry lower alkanol vapour (water content not more than 5 mole %) is injected into the bottom of the column reactor. 3. Water of esterification is removed from the top of the column reactor in the vapour stream, whilst ester product is recovered from the sump of the reactor.
Oleochemicals - What are they?
fatty acids
fatty alcohols
fatty methyl esters
fatty amines
glycerine
Oleochemical pathways
What are they used for?
Where do they come from?
Review of Organic Functional Groups
Fatty Acids
- Uses
- Process
- Splitting
- Hydrogenation
Ni Catalyst for FA hydrogenation
Catalyst deactivation in fatty acids by corrosion
Ni soap decomposition
Nickel dissolution in the presence of hydrogen
Comparison pore size & TG/FA molecules
Effect of pore dimensions in fatty acid hardening
Effect of premixing timeon catalyst activity
Effects of catalyst dissolution summarized:
Reducing Ni soaps
Issues
Alternative catalyst for FA hydrogenation (i)
Precious metal catalyst cycle
Alternative catalyst for FA hydrogenation (ii)
Fatty Alcohols
- Uses
- Process
Fatty Ester Hydrogenolysis
Fixed Bed Hydrogenolysis
Slurry Phase Hydrogenolysis
Fatty OH polishing
Fatty Methyl Esters
- Uses
Advantages of ME vs FA as a feedstock
FME - Biodiesel
Fatty Amines
Glycerin
- Uses
- The Future
REFERENCE:
Some graphs and photographs, in particular the photo of "The nickel deposits in the tube section", were extracted from Johnson Matthey contributions to International conferences.
Episode 46 : PRODUCTION OF OLEOCHEMICAL METHYL ESTER FROM RBD PALM KERNEL OIL SAJJAD KHUDHUR ABBAS
Episode 46 : PRODUCTION OF OLEOCHEMICAL METHYL ESTER FROM
RBD PALM KERNEL OIL
Oleo chemicals
The term ― oleo chemicals refers to any chemical compounds derived from natural oils
almost 95% of natural oils and fats are used in food application
small percentage is applied in non-food purposes such as soap manufacturing
The advantages of using oleo chemicals over petrochemicals are:
Oleo chemicals are derived from renewable resources .
Oleo chemical production requires less energy and causes less pollution .
Oleo chemicals are fully non-toxic .
SAJJAD KHUDHUR ABBAS
Ceo , Founder & Head of SHacademy
Chemical Engineering , Al-Muthanna University, Iraq
Oil & Gas Safety and Health Professional – OSHACADEMY
Trainer of Trainers (TOT) - Canadian Center of Human
Development
Fatty alcohol. Define fatty alcohols Describe the production processes of fatty alcohols and its derivatives Draw the flow chart of fatty alcohol production Explain the uses and application of fatty alcohols.
3. Definitionof Fatty Alcohols Fatty alcohols are the workhorse raw materials that facilitate the existence of products such as shampoos, shaving creams, laundry detergents, etc, and are produced at a rate of about one-and-a-half million tonnes per year and growing. Fatty alcohols are oleochemicals derived from vegetable feedstocks. The feedstock raw materials include coconut and palm kernel oils. These refined vegetable oils are first converted to a methyl ester or fatty acid. This reaction generates crude glycerine. The intermediate methyl ester or fatty acid are then fractionated and hydrogenated to produce fatty alcohol. Sources : http://www.pgchemicals.com/products/fatty-alcohols/
4. Chemical Equation for Fatty Alcohol Production Sources : http://www.pgchemicals.com/products/fatty- alcohols/
5. Block diagram of Fatty Alcohol production process
6. Fatty acids are converted into methyl ester and hydrogenated into fatty alcohols.
7. Sources : http://www.abq.org.br/workshop/11/ADRIANO- SALES-%20FIRJAM_Oleochemicals-from-Palm-Kernel- Oil.pdf
8. Hydrogenation All natural fatty alcohol processes are based on renewable fats and oils like coconut, palm oil,palm kernel,rope seed and soya bean oil. It has been proven that hydrogenation of methyl esters are preferred alternatives than hydrogenating the oils directly. Using fixed bed hydrogenation process offers the advantage of lower hydrogenation temperatures and pressures. Using special catalysts, this process is able to produce unsaturated fatty alcohols too. To produce fatty alcohols, there are three routes which is acid route,ester route and wax ester route that are shown in the following block diagrams.
9. - Acid route - Ester route - Wax ester route
10. Acid Route
Presented by: Dr. Adel Gabr Abdel-Razek
Fats and Oils Dept., National Research Center.
in workshop on Workshop on Oleochemicals at the SemiRamis Intercontinental Hotel.
Sources of fatty amines
The natural reaction pathways of fatty amines
Manufacture of hetero-alkyl amines
tertiary amines
quaternary amine salts
Directional influence of H2, NH3 and H2O on:
amine distribution
conversion and reaction rate
Oleochemical Technology. Production of fatty acids & glycerine starting from vegetable & animal oil and fats Hydrolysis is the basic production step, the fats and oils are split into crude glycerine and a mixture of crude fatty acids, under the combined action of water, temperature and pressure. The temperature exceeds 200°C and the products are kept under pressure for more than 20 minutes.. Fats & oils crude glycerine + crude fatty acids + water
3. • A process for the esterification of a triglyceride. • The process comprises forming a single phase solution of said triglyceride in an alcohol selected from methanol and ethanol, the ratio of alcohol to triglyceride being 15:1 to 35:1. • The solution further comprises a co-solvent in an amount to effect formation the single phase and a base catalyst for the esterification reaction. • After a period of time, ester is recovered from the solution. • Esterification is rapid and proceeds essentially to completion. • The esters may be used as biofuel or biodiesel
4. Glycerine (also called glycerin or glycerol) is an alcohol which is used as a moisturizer in soaps and lotions. Glycerine has a sweet taste, and it can be used as a food preservative and a non-sugar sweetener.
5. Glycerine Lubricants (jet engine, refrigeration) Plasticizer for Polyvinyl Butyral (PVB) Explosives Polyurethane Foam
6. Examples of Derivative
7. Process involves 1. A fatty acid or fatty acid mixture is esterified in a column reactor. 4. As the liquid flows down the trays it encounters progressively drier lower alkanol. 5. The ester product recovered from the bottom of the reactor has an ester content of at least 99 mole % (calculated on a lower alkanol free basis). 2. Relatively dry lower alkanol vapour (water content not more than 5 mole %) is injected into the bottom of the column reactor. 3. Water of esterification is removed from the top of the column reactor in the vapour stream, whilst ester product is recovered from the sump of the reactor.
Oleochemicals - What are they?
fatty acids
fatty alcohols
fatty methyl esters
fatty amines
glycerine
Oleochemical pathways
What are they used for?
Where do they come from?
Review of Organic Functional Groups
Fatty Acids
- Uses
- Process
- Splitting
- Hydrogenation
Ni Catalyst for FA hydrogenation
Catalyst deactivation in fatty acids by corrosion
Ni soap decomposition
Nickel dissolution in the presence of hydrogen
Comparison pore size & TG/FA molecules
Effect of pore dimensions in fatty acid hardening
Effect of premixing timeon catalyst activity
Effects of catalyst dissolution summarized:
Reducing Ni soaps
Issues
Alternative catalyst for FA hydrogenation (i)
Precious metal catalyst cycle
Alternative catalyst for FA hydrogenation (ii)
Fatty Alcohols
- Uses
- Process
Fatty Ester Hydrogenolysis
Fixed Bed Hydrogenolysis
Slurry Phase Hydrogenolysis
Fatty OH polishing
Fatty Methyl Esters
- Uses
Advantages of ME vs FA as a feedstock
FME - Biodiesel
Fatty Amines
Glycerin
- Uses
- The Future
REFERENCE:
Some graphs and photographs, in particular the photo of "The nickel deposits in the tube section", were extracted from Johnson Matthey contributions to International conferences.
Episode 46 : PRODUCTION OF OLEOCHEMICAL METHYL ESTER FROM RBD PALM KERNEL OIL SAJJAD KHUDHUR ABBAS
Episode 46 : PRODUCTION OF OLEOCHEMICAL METHYL ESTER FROM
RBD PALM KERNEL OIL
Oleo chemicals
The term ― oleo chemicals refers to any chemical compounds derived from natural oils
almost 95% of natural oils and fats are used in food application
small percentage is applied in non-food purposes such as soap manufacturing
The advantages of using oleo chemicals over petrochemicals are:
Oleo chemicals are derived from renewable resources .
Oleo chemical production requires less energy and causes less pollution .
Oleo chemicals are fully non-toxic .
SAJJAD KHUDHUR ABBAS
Ceo , Founder & Head of SHacademy
Chemical Engineering , Al-Muthanna University, Iraq
Oil & Gas Safety and Health Professional – OSHACADEMY
Trainer of Trainers (TOT) - Canadian Center of Human
Development
Fatty alcohol. Define fatty alcohols Describe the production processes of fatty alcohols and its derivatives Draw the flow chart of fatty alcohol production Explain the uses and application of fatty alcohols.
3. Definitionof Fatty Alcohols Fatty alcohols are the workhorse raw materials that facilitate the existence of products such as shampoos, shaving creams, laundry detergents, etc, and are produced at a rate of about one-and-a-half million tonnes per year and growing. Fatty alcohols are oleochemicals derived from vegetable feedstocks. The feedstock raw materials include coconut and palm kernel oils. These refined vegetable oils are first converted to a methyl ester or fatty acid. This reaction generates crude glycerine. The intermediate methyl ester or fatty acid are then fractionated and hydrogenated to produce fatty alcohol. Sources : http://www.pgchemicals.com/products/fatty-alcohols/
4. Chemical Equation for Fatty Alcohol Production Sources : http://www.pgchemicals.com/products/fatty- alcohols/
5. Block diagram of Fatty Alcohol production process
6. Fatty acids are converted into methyl ester and hydrogenated into fatty alcohols.
7. Sources : http://www.abq.org.br/workshop/11/ADRIANO- SALES-%20FIRJAM_Oleochemicals-from-Palm-Kernel- Oil.pdf
8. Hydrogenation All natural fatty alcohol processes are based on renewable fats and oils like coconut, palm oil,palm kernel,rope seed and soya bean oil. It has been proven that hydrogenation of methyl esters are preferred alternatives than hydrogenating the oils directly. Using fixed bed hydrogenation process offers the advantage of lower hydrogenation temperatures and pressures. Using special catalysts, this process is able to produce unsaturated fatty alcohols too. To produce fatty alcohols, there are three routes which is acid route,ester route and wax ester route that are shown in the following block diagrams.
9. - Acid route - Ester route - Wax ester route
10. Acid Route
Presented by: Dr. Adel Gabr Abdel-Razek
Fats and Oils Dept., National Research Center.
in workshop on Workshop on Oleochemicals at the SemiRamis Intercontinental Hotel.
The document is a project report for manufacturing MEA TRIAZINE from paraformaldehyde and monoethanol amine. MEA TRIAZINE is used as H2S scavanger in crude oilfields.
Natural Gas (from a natural reservoir or associated to a crude production) can contain acid gas (H2S and/or CO2)..
The Gas Sweetening Process aims to remove part or all of the acid gas.
Narrow Range Ethoxylates - Highly targeted performance for more effective cle...Sorel Muresan
A narrow range ethoxylated alcohol, also called “a peaked ethoxylate”, has a distribution curve that is narrower than the equivalent standard alcohol ethoxylate with a considerably lower content of unreacted alcohol and lower foam than standard ethoxylates. Narrow range ethoxylates have targeted properties to improve degreasing performance at lower use concentration, while eliminating the need for hazardous solvents. At the same time they are compatible with most commonly used surfactants and builders. They also have very low odor, even if based on a short chain alcohol. This opens up many applications where short chain alcohol ethoxylates have previously been excluded and enables the formulator to prepare highly effective low VOC cleaners. The lower free alcohol content and higher proportion of the target ethoxylate make formulating easier and more cost effective than with standard alcohol ethoxylates. This offers the possibility to optimize raw material purchase, reduce inventories, and simplify production.
Acetylene Hydrogenation - Consultancy
Ethylene Plant Flowsheets
Placement of Acetylene Hydrogenation Reactor
Cracker Feedstock / Product Variability
Acetylene Reactor Feeds
Reasons for Acetylene Removal
Reacting Components and Conditions
Reactor Operation and Reacting Components
Reactor Design
Selectivity vs. Temperature and Ethane Formation
Effect of CO
Poisons
Green Oil
Turndown
H/D Ratio and Pressure Drop
Thermocouple Placement
Start-up
Problems During Start-up
Shut Down
Regeneration
Catalyst Experience, Problems and Other Information
Front End / Tail End Comparison
The document is a project report for manufacturing MEA TRIAZINE from paraformaldehyde and monoethanol amine. MEA TRIAZINE is used as H2S scavanger in crude oilfields.
Natural Gas (from a natural reservoir or associated to a crude production) can contain acid gas (H2S and/or CO2)..
The Gas Sweetening Process aims to remove part or all of the acid gas.
Narrow Range Ethoxylates - Highly targeted performance for more effective cle...Sorel Muresan
A narrow range ethoxylated alcohol, also called “a peaked ethoxylate”, has a distribution curve that is narrower than the equivalent standard alcohol ethoxylate with a considerably lower content of unreacted alcohol and lower foam than standard ethoxylates. Narrow range ethoxylates have targeted properties to improve degreasing performance at lower use concentration, while eliminating the need for hazardous solvents. At the same time they are compatible with most commonly used surfactants and builders. They also have very low odor, even if based on a short chain alcohol. This opens up many applications where short chain alcohol ethoxylates have previously been excluded and enables the formulator to prepare highly effective low VOC cleaners. The lower free alcohol content and higher proportion of the target ethoxylate make formulating easier and more cost effective than with standard alcohol ethoxylates. This offers the possibility to optimize raw material purchase, reduce inventories, and simplify production.
Acetylene Hydrogenation - Consultancy
Ethylene Plant Flowsheets
Placement of Acetylene Hydrogenation Reactor
Cracker Feedstock / Product Variability
Acetylene Reactor Feeds
Reasons for Acetylene Removal
Reacting Components and Conditions
Reactor Operation and Reacting Components
Reactor Design
Selectivity vs. Temperature and Ethane Formation
Effect of CO
Poisons
Green Oil
Turndown
H/D Ratio and Pressure Drop
Thermocouple Placement
Start-up
Problems During Start-up
Shut Down
Regeneration
Catalyst Experience, Problems and Other Information
Front End / Tail End Comparison
introduction to soil stabilization and introduction to geo textiles and synth...husna004
Stabilization is the process of blending and mixing materials with a soil to improve certain properties of the soil. The process may include the blending of soils to achieve a desired gradation or the mixing of commercially available additives that may alter the gradation, texture or plasticity, or act as a binder for cementation of the soil.
Pressure Relief Systems Vol 2
Causes of Relief Situations
This Volume 2 is a guide to the qualitative identification of common causes of overpressure in process equipment. It cannot be exhaustive; the process engineer and relief systems team should look for any credible situation in addition to those given in this Part which could lead to a need for pressure relief (a relief situation).
Pressure Relief Systems
BACKGROUND TO RELIEF SYSTEM DESIGN Vol.1 of 6
The Guide has been written to advise those involved in the design and engineering of pressure relief systems. It takes the user from the initial identification of potential causes of overpressure or under pressure through the process design of relief systems to the detailed mechanical design. "Hazard Studies" and quantitative hazards analysis are not described; these are seen as complementary activities. Typical users of the Guide will use some Parts in detail and others in overview.
GAS DISPERSION - A Definitive Guide to Accidental Releases of Heavy GasesGerard B. Hawkins
GAS DISPERSION - A Definitive Guide to Accidental Releases of Heavy Gases
This Process Safety Guide has been written with the aim of assisting process engineers, hazard analysts and environmental advisers in carrying out gas dispersion calculations. The Guide aims to provide assistance by:
• Improving awareness of the range of dispersion models available within GBHE, and providing guidance in choosing the most appropriate model for a particular application.
• Providing guidance to ensure that source terms and other model inputs are correctly specified, and the models are used within their range of applicability.
• Providing guidance to deal with particular topics in gas dispersion such as dense gas dispersion, complex terrain, and modeling the chemistry of oxides of nitrogen.
• Providing general background on air quality and dispersion modeling issues such as meteorology and air quality standards.
• Providing example calculations for real practical problems.
SCOPE
The gas dispersion guide contains the following Parts:
1 Fundamentals of meteorology.
2 Overview of air quality standards.
3 Comparison between different air quality models.
4 Designing a stack.
5 Dense gas dispersion.
6 Calculation of source terms.
7 Building wake effects.
8 Overview of the chemistry of the oxides of nitrogen.
9 Overview of the ADMS complex terrain module.
10 Overview of the ADMS deposition module.
11 ADMS examples.
12 Modeling odorous releases.
13 Bibliography of useful gas dispersion books and reports.
14 Glossary of gas dispersion modeling terms.
Appendix A : Modeling Wind Generation of Particulates.
APPENDIX B TABLE OF PROPERTY VALUES FOR SPECIFIC CHEMICALS
Theory of Carbon Formation in Steam Reforming
Contents
1 Introduction
2 Underpinning Theory
2.1 Conceptualization
2.2 Reforming Reactions
2.3 Carbon Formation Chemistry
2.3.1 Natural Gas
2.3.2 Carbon Formation for Naphtha Feeds
2.3.3 Carbon Gasification
2.4 Heat Transfer
3 Causes
3.1 Effects of Carbon Formation
3.2 Types of Carbon
4 What are the Effects of Carbon Formation?
4.1 Why does Carbon Formation Get Worse?
4.1.1 So what is the Next Step?
4.2 Consequences of Carbon Formation
4.3 Why does Carbon Form where it does?
4.3.1 Effect on Process Gas Temperature
4.4 Why does Carbon Formation Propagate Down the Tube?
4.4.1 Effect on Radiation on the Fluegas Side
4.5 Why does Carbon Formation propagate Up the Tube?
5 How do we Prevent Carbon Formation
5.1 The Role of Potash
5.2 Inclusion of Pre-reformer
5.3 Primary Reformer Catalyst Parameters
5.3.1 Activity
5.3.2 Heat Transfer
5.3.3 Increased Steam to Carbon Ratio
6 Steam Out
6.1 Why does increasing the Steam to Carbon Ratio Not Work?
6.2 Why does reducing the Feed Rate not help?
6.3 Fundamental Principles of Steam Outs
TABLES
1 Heat Transfer Coefficients in a Typical Reformer
2 Typical Catalyst Loading Options
FIGURES
1 Hot Bands
2 Conceptual Pellet
3 Naphtha Carbon Formation
4 Heat Transfer within an Reformer
5 Types of Carbon Formation
6 Effect of Carbon on Nickel Crystallites
7 Absorption of Heat
8 Comparison of "Base Case" v Carbon Forming Tube
9 Carbon Formation Vicious Circle
10 Temperature Profiles
11 Carbon Pinch Point
12 Carbon Formation
13 Effect on Process Gas Temperature
14 How does Carbon Propagate into an Unaffected Zone?
15 Movement of the Carbon Forming Region
16 Effect of Hot Bands on Radiative Heat Transfer
17 Effect of Potash on Carbon Formation
18 Application of a Pre-reformer
19 Effect of Activity on Carbon Formation
Calculation of an Ammonia Plant Energy Consumption: Gerard B. Hawkins
Calculation of an Ammonia Plant Energy Consumption:
Case Study: #06023300
Plant Note Book Series: PNBS-0602
CONTENTS
0 SCOPE
1 CALCULATION OF NATURAL GAS PROCESS FEED CONSUMPTION
2 CALCULATION OF NATURAL GAS PROCESS FUEL CONSUMPTION
3 CALCULATION OF NATURAL GAS CONSUMPTION FOR PILOT BURNERS OF FLARES
4 CALCULATION OF DEMIN. WATER FROM DEMIN. UNIT
5 CALCULATION OF DEMIN. WATER TO PACKAGE BOILERS
6 CALCULATION OF MP STEAM EXPORT
7 CALCULATION OF LP STEAM IMPORT
8 DETERMINATION OF ELECTRIC POWER CONSUMPTION
9 DETERMINATION OF THE TOTAL ENERGY CONSUMPTION OF THE AMMONIA PLANT ISBL
10 ADJUSTMENT OF ELECTRIC POWER CONSUMPTION FOR TEST RUN CONDITIONS
11 CALCULATION OF AMMONIA SHARE IN MP STEAM CONSUMPTION IN UTILITIES
12 CALCULATION OF AMMONIA SHARE IN ELECTRIC POWER CONSUMPTION IN UTILITIES
13 DETERMINATION OF THE TOTAL ENERGY CONSUMPTION OF THE AMMONIA PLANT OSBL
14 DETERMINATION OF THE TOTAL ENERGY CONSUMPTION OF THE AMMONIA PLANT
Ammonia Plant Technology
Pre-Commissioning Best Practices
GBHE-APT-0102
PICKLING & PASSIVATION
CONTENTS
1 PURPOSE OF THE WORK
2 CHEMICAL CONCEPT
3 TECHNICAL CONCEPT
4 WASTES & SAFETY CONCEPT
5 TARGET RESULTS
6 THE GENERAL CLEANING SEQUENCE MANAGEMENT
6.6.1 Pre-cleaning or “Physical Cleaning
6.6.2 Pre-rinsing
6.6.3 Chemical Cleaning
6.6.4 Critical Factors in Cleaning Success
6.6.5 Rinsing
6.6.6 Inspection and Re-Cleaning, if Necessary
7 Systems to be treated by Pickling/Passivation
Ammonia Plant Technology
Pre-Commissioning Best Practices
Piping and Vessels Flushing and Cleaning Procedure
CONTENTS
1 Scope
2 Aim/purpose
3 Responsibilities
4 Procedure
4.1 Main cleaning methods
4.1.1 Mechanical cleaning
4.1.2 Cleaning with air
4.1.3 Cleaning with steam (for steam networks only)
4.1.4 Cleaning with water
4.2 Choice of the cleaning method
4.3 Cleaning preparation
4.4 Protection of the devices included in the network
4.5 Protection of devices in the vicinity of the network
4.6 Water flushing procedure
4.6.1 Specific problems of water flushing
4.6.2 Preparation for water flushing
4.6.3 Performing a water flush
4.6.4 Cleanliness criteria
4.7 Air blowing procedure
4.7.1 Specific problems of air blowing
4.7.2 Preparation for air blowing
4.7.3 Performing air blowing
4.7.4 Cleanliness checks
4.8 Steam blowing procedure
4.8.1 Specific problems of steam blowing
4.8.2 Preparation for steam blowing
4.8.3 Performing steam blowing
4.8.4 Cleanliness checks
4.9 Chemical cleaning procedure
4.9.1 Specific problems of cleaning with a chemical solution
4.9.2 Preparation for chemical cleaning
4.9.3 Performing a chemical cleaning
4.9.4 Cleanliness criteria
4.10 Re-assembly - general guideline
4.11 Preservation of flushed piping
DESIGN OF VENT GAS COLLECTION AND DESTRUCTION SYSTEMS Gerard B. Hawkins
DESIGN OF VENT GAS COLLECTION AND DESTRUCTION SYSTEMS
CONTENTS
1 INTRODUCTION
1.1 Purpose
1.2 Scope of this Guide
1.3 Use of the Guide
2 ENVIRONMENTAL ISSUES
2.1 Principal Concerns
2.2 Mechanisms for Ozone Formation
2.3 Photochemical Ozone Creation Potential
2.4 Health and Environmental Effects
2.5 Air Quality Standards for Ground Level Concentrations of Ozone, Targets for Reduction of VOC Discharges and Statutory Discharge Limits
3 VENTS REDUCTION PHILOSOPHY
3.1 Reduction at Source
3.2 End-of-pipe Treatment
4 METHODOLOGY FOR COLLECTION & ASSESSMENT OF PROCESS FLOW DATA
4.1 General
4.2 Identification of Vent Sources
4.3 Characterization of Vents
4.4 Quantification of Process Vent Flows
4.5 Component Flammability Data Collection
4.6 Identification of Operating Scenarios
4.7 Quantification of Flammability Characteristics for Combined Vents
4.8 Identification, Quantification and Assessment of Possibility of Air Ingress Routes
4.9 Tabulation of Data
4.10 Hazard Study and Risk Assessment
4.11 Note on Aqueous / Organic Wastes
4.12 Complexity of Systems
4.13 Summary
5 SAFE DESIGN OF VENT COLLECTION HEADER SYSTEMS
5.1 General
5.2 Process Design of Vent Headers
5.3 Liquid in Vent Headers
5.4 Materials of Construction
5.5 Static Electricity Hazard
5.6 Diversion Systems
5.7 Snuffing Systems
6 SAFE DESIGN OF THERMAL OXIDISERS
6.1 Introduction
6.2 Design Basis
6.3 Types of High Temperature Thermal Oxidizer
6.4 Refractories
6.5 Flue Gas Treatment
6.6 Control and Safety Systems
6.7 Project Program
6.8 Commissioning
6.9 Operational and Maintenance Management
APPENDICES
A GLOSSARY
B FLAMMABILITY
C EXAMPLE PROFORMA
D REFERENCES
DOCUMENTS REFERRED TO IN THIS PROCESS GUIDE
TABLE
1 PHOTOCHEMICAL OZONE CREATION POTENTIAL REFERENCED
TO ETHYLENE AS UNITY
FIGURES
1 SCHEMATIC OF TYPICAL VENT COLLECTION AND THERMAL OXIDIZER SYSTEM
2 TYPICAL KNOCK-OUT POT WITH LUTED DRAIN
3 SCHEMATIC OF DIVERSION SYSTEM
4 CONVENTIONAL VERTICAL THERMAL OXIDIZER
5 CONVENTIONAL OXIDIZER WITH INTEGRAL WATER SPARGER
6 THERMAL OXIDIZER WITH STAGED AIR INJECTION
7 DOWN-FIRED UNIT WITH WATER BATH QUENCH
8 FLAMELESS THERMAL OXIDATION UNIT
9 THERMAL OXIDIZER WITH REGENERATIVE HEAT RECOVERY
10 TYPICAL PROJECT PROGRAM
11 TYPICAL FLAMMABILITY DIAGRAM
12 EFFECT OF DILUTION WITH AIR
13 EFFECT OF DILUTION WITH AIR ON 100 Rm³ OF FLAMMABLE GAS
PRACTICAL GUIDE ON THE SELECTION OF PROCESS TECHNOLOGY FOR THE TREATMENT OF A...Gerard B. Hawkins
PRACTICAL GUIDE ON THE SELECTION OF PROCESS TECHNOLOGY FOR THE TREATMENT OF AQUEOUS ORGANIC EFFLUENT STREAMS
CONTENTS
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
3.1 IPU
3.2 AOS
3.3 BODs
3.4 COD
3.5 TOC
3.6 Toxicity
3.7 Refractory Organics/Hard COD
3.8 Heavy Metals
3.9 EA
3.10 Biological Treatment Terms
3.11 BATNEEC
3.12 BPEO
3.13 EQS/LV
3.14 IPC
3.15 VOC
3.16 F/M Ratio
3.17 MLSS
3.18 MLVSS
4 DESIGN/ECONOMIC GUIDELINES
5 EUROPEAN LEGISLATION
5.1 General
5.2 Integrated Pollution Control (IPC)
5.3 Best Available Techniques Not Entailing Excessive Costs (BATNEEC)
5.4 Best Practicable Environmental Option (BPEO)
5.5 Environmental Quality Standards(EQS)
6 IPU EXIT CONCENTRATION
7 SITE/LOCAL REQUIREMENTS
8 PROCESS SELECTION PROCEDURE
8.1 Waste Minimization Techniques (WMT)
8.2 AOS Stream Definition
8.3 Technical Check List
8.4 Preliminary Selection of Suitable Technologies
8.5 Process Sequences
8.6 Economic Evaluation
8.7 Process Selection
APPENDICES
A DIRECTIVE 76/464/EEC - LIST 1
B DIRECTIVE 76/464/EEC - LIST 2
C THE EUROPEAN COMMISSION PRIORITY CANDIDATE LIST
D THE UK RED LIST
E CURRENT VALUES FOR EUROPEAN COMMUNITY ENVIRONMENTAL QUALITY STANDARDS AND CORRESPONDING LIMIT VALUES
F ESTABLISHED TECHNOLOGIES
G EMERGING TECHNOLOGY
H PROPRIETARY/LESS COMMON TECHNOLOGIES
J COMPARATIVE COST DATA
PRACTICAL GUIDE ON THE REDUCTION OF DISCHARGES TO ATMOSPHERE OF VOLATILE ORGA...Gerard B. Hawkins
PRACTICAL GUIDE ON THE REDUCTION OF DISCHARGES TO ATMOSPHERE OF VOLATILE ORGANIC COMPOUNDS (VOCs)
FOREWORD
CONTENTS
1 INTRODUCTION
2 THE NEED FOR VOC CONTROL
3 CONTROL AT SOURCE
3.1 Choice or Solvent
3.2 Venting Arrangements
3.3 Nitrogen Blanketing
3.4 Pump Versus Pneumatic Transfer
3.5 Batch Charging
3.6 Reduction of Volumetric Flow
3.7 Stock Tank Design
4 DISCHARGE MEASUREMENT
4.1 By Inference or Calculation
4.2 Flow Monitoring Equipment
4.3 Analytical Instruments
4.4 Vent Emissions Database
5 ABATEMENT TECHNOLOGY
5.1 Available Options
5.2 Selection of Preferred Option
5.3 Condensation
5.4 Adsorption
5.5 Absorption
5.6 Thermal Incineration
5.7 Catalytic Oxidation
5.8 Biological Filtration
5.9 Combinations of Process technologies
5.10 Processes Under Development
6 GLOSSARY OF TERMS
7 REFERENCES
Appendix 1. Photochemical Ozone Creation Potentials
Appendix 2. Examples of Adsorption Preliminary Calculations
Appendix 3. Example of Thermal Incineration Heat and Mass Balance
Appendix 4. Cost Correlations
Getting the Most Out of Your Refinery Hydrogen PlantGerard B. Hawkins
Getting the Most Out of Your Refinery Hydrogen Plant
Contents
Summary
1 Introduction
2 "On-purpose" Hydrogen Production
3 Operational Aspects
4 Uprating Options on the Steam Reformer
4.1 Steam Reforming Catalysts and Tube Metallurgy
4.2 Oxygen-blown Secondary Reformer
4.3 Pre-reforming
4.4 Post-reforming
5 Downstream Units
6 Summary of Uprating Options
7 Conclusions
EMERGENCY ISOLATION OF CHEMICAL PLANTS
CONTENTS
1 Introduction
2 When should Emergency Isolation Valves be Installed
3 Emergency Isolation Valves and Associated Equipment
3.1 Installations on existing plant
3.2 Actuators
3.3 Power to close or power to open
3.4 The need for testing
3.5 Hand operated Emergency Valves
3.6 The need to stop pumps in an emergency
3.7 Location of Operating Buttons
3.8 Use of control valves for Isolation
4 Detection of Leaks and Fires
5 Precautions during Maintenance
6 Training Operators to use Emergency Isolation Valves
7 Emergency Isolation when no remotely operated valve is available
References
Glossary
Appendix I Some Fires or Serious Escapes of Flammable Gases or Liquids that could have been controlled by Emergency Isolation Valves
Appendix II Some typical Installations
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Amine Gas Treating Unit Best Practices - Troubleshooting Guide for H2S/CO2 Amine Systems
Contents
Process Capabilities for gas treating process
Typical Amine Treating
Typical Amine System Improvements
Primary Equipment Overview
Inlet Gas Knockout
Absorber
Three Phase Flash Tank
Lean/Rich Heat Exchanger
Regenerator
Filtration
Amine Reclaimer
Operating Difficulties Overview
Foaming
Failure to Meet Gas Specification
Solvent Losses
Corrosion
Typical Amine System Improvements
Degradation of Amines and Alkanolamines during Sour Gas Treating
APPENDIX
Best Practices - Troubleshooting Guide
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Clipboard AI
GenAI applicata alla Document Understanding
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Topics covered:
UI automation Introduction,
UI automation Sample
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Key Trends Shaping the Future of Infrastructure.pdfCheryl Hung
Keynote at DIGIT West Expo, Glasgow on 29 May 2024.
Cheryl Hung, ochery.com
Sr Director, Infrastructure Ecosystem, Arm.
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While the dev and ops silo continues to crumble….many organizations still relegate monitoring & observability as the purview of ops, infra and SRE teams. This is a mistake - achieving a highly observable system requires collaboration up and down the stack.
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2. Most uses depend on the cationic nature of the amine
Fatty
Amines
Corrosion
Inhibitors
Fabric
Softeners
Lubricant
Additive
Organoclays
Sanitizing
Agents
H
H
NR
6. Batch slurry phase most common
Fixed bed or continuous slurry phase also used
Product Temp (C)
Pressure
(bar)
Catalysts Special Conditions
Primary 80-150 10-550
nickel, raney
nickel, cobalt
Ammonia added to feed to suppress
secondary and tertiary amine formation
Secondary 150-200 50-200 nickel, cobalt Ammonia removed by purging with hydrogen
Tertiary 160-230 7 - 14 nickel, cobalt
Secondary Amine used as feed; hydrogen
purge necessary to remove ammonia
Unsaturated
copper
chromite,
nickel
powder
similar to abovesimilar to above
14. Tertiary amine formation
proceeds via the same route as
with the secondary amine
formation. However, secondary
amine condenses with imine to
yield tertiary intermediates.
15. Amine Catalyst
Saturated Primary Amine Sponge Ni type catalyst
Unsaturated Primary Amine Supported Ni powder catalysts, Supported Co tablet catalysts
Saturated Secondary Amines Supported Ni powder catalysts
Unsaturated Secondary Amines Supported Ni powder catalysts
Tertiary Amines Supported Ni powder catalysts