BENFIELD LIQUOR: DETERMINATION OF IRON
SCOPE AND FIELD OF APPLICATION
This method is suitable for the determination of the total iron in Benfield liquor samples up to a concentration of approximately 100 ppm m/v.
Determination of Hydrogen Sulfide by Cadmium Sulfide PrecipitationGerard B. Hawkins
Plant Analytical Techniques
Gas Analysis: Determination of Hydrogen Sulfide by Cadmium Sulfide Precipitation
SCOPE AND FIELD OF APPLICATION
This method is suitable for the in situ determination of hydrogen sulfide in ammonia plant gas streams when testing is required during catalyst reduction.
PRINCIPLE
Hydrogen sulfide present in the gas precipitates cadmium sulfide from a cadmium solution. The precipitate is filtered then reacted with iodine; the excess iodine is then titrated with sodium thiosulfate.
Physical properties and thermochemistry for reactor technologyGerard B. Hawkins
Physical Properties and Thermochemistry for Reactor Technology
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 PHYSICAL PROPERTIES
4.1 Form of Equations
4.2 The Physical Property System: “The VAULT”
4.3 Physical Property Programs
4.4 Physical Property Estimation
4.5 Sources of Expertise
5 INTERFACING COMPUTER PROGRAMS TO THE
GBHE VAULT PHYSICAL PROPERTIES PACKAGE
5.1 Preparation of the Physical Property Data
6 THERMOCHEMISTRY
6.1 Hess's Law
6.2 Standard States
6.3 Heats of Formation
6.4 Determination of Heats of Reaction
7 CALCULATION OF HEATS OF REACTION
7.1 Analogous Reactions
7.2 Heat of Formation Data Compilations
7.3 Estimation of Standard Heats of Formation
7.4 Heats of Neutralization
7.5 Temperature Effect on Heat of Reaction
8 HEATS OF SOLUTION, DILUTION AND MIXING
8.1 Calculation of Heats of Solution / Dilution from
Literature Data
8.2 Estimation of Heats of Solution and Mixing
8.3 Integral and Differential Heats
9 EXPERIMENTAL DETERMINATION OF
THERMOCHEMICAL PARAMETERS
9.1 Isoperibol Calorimetry for Heats of Reaction and Solution
9.2 Heat Flow Calorimetry
9.3 Adiabatic Calorimeter
9.4 Differential Scanning Calorimetry
10 COMPUTER CALCULATION OF ENTHALPY OR
TEMPERATURE
11 BIBLIOGRAPHY
Biological Systems: A Special Case
Up till now we have discussed various aspects of the separation and processing of fine solids without too much reference (except in the examples) to the specifics of the properties of the materials concerned. Though the material properties are the dominant influence on efficient process design and operation, it has been postulated that the necessary characteristics for process selection and optimization can be found fairly readily using easily-applicable rheological and other techniques. This underlying assumption also seems to hold good for biological suspensions; however, certain aspects of the behavior of these systems are sufficiently specialized for them to merit a separate discussion viz:
1 TYPES OF BIOLOGICAL SEPARATION
1.1 Whole-Organism Case
1.2 Part-Cell Separations
1.3 Isolation of Individual Molecular Species
2 SETTING ABOUT DEVISING AN EFFECTIVE
PROCESS FOR SEPARATION OF A BIOLOGICAL MATERIAL
2.1 Whole-Organism Case
2.1.1 Characterization of Biopolymers in the Liquor
2.1.2 Release of Internal Water
2.2 Part -Cell Separations
2.2.1 Selectivity
2.2.2 Cost
2.3 Isolation of Individual Molecular Species
3 Examples
3.1 Effective Design and Operation of a Process for Harvesting of Single Cell Protein
3.2 Harvesting of Mycoprotein for Human Consumption
3.3 Thickening of a Filamentous Organism Suspension
3.4 Separation of Poly-3-hydroxybutyrate Polymer (PHB) from Alcaligenes Eutrophus Biomass
3.5 Isolation of Organic Acid Produced by an Enzymatic Process
4 REFERENCES
Table
Figures
GE / Texaco Gasifier Feed to a Lurgi Methanol Plant and its Effect on Methano...Gerard B. Hawkins
GE / Texaco Gasifier Feed to a Lurgi Methanol Plant and its Effect on Methanol Production
CONTENTS
0 Methanol Synthesis Introduction
1 Executive Summary
2 Design Basis
2.1.1 Train I Design Basis
2.1.2 Train II Design Basis
2.1.3 Train III Design Basis
2.2 Design Philosophy
2.2.1 Operability Review
2.3 Assumptions
2.4 Train IV Flowsheet
2.4.1 CO2 Removal
3 Discussion
3.1 Natural Gas Consumption Figures
3.1.1 Base Case
3.1.2 Case 1 – Coal Gasification in Service
3.1.3 Case 2 – Coal Gasification in Service – No CO2 Export
3.2 Methanol Production Figures
3.2.1 Base Case
3.2.2 Case 1 – Coal Gasification in Service
3.2.3 Case 2 – Coal Gasification in Service – No CO2 Export
3.3 85% Natural Gas Availability
3.4 100% Natural Gas Availability
3.5 CO2 Emissions
3.5.1 Base Case
3.5.2 Case 1 – Coal Gasification in Service
3.5.3 Case 2 – Coal Gasification in Service – No CO2 Export
3.6 Specific Consumption Figures
3.6.1 Base Case
3.6.2 Case 1 – Coal Gasification and CO2 Import
3.6.3 Case 2 – Coal Gasification and No CO2 Import
3.7 Train IV Synthesis Gas Composition
4 Further Work
5 Conclusion
APPENDIX
Important Stream Data – Material Balance Stream Data
Texaco Gasifier with HP Steam Raising Boiler
CHARACTERISTICS OF COAL
Material Balance Considerations
High Temperature Shift Catalyst Reduction ProcedureGerard B. Hawkins
High Temperature Shift Catalyst Reduction Procedure
The catalyst, as supplied, is Fe2O3. This reduces to the active form, Fe3O4, in the presence of hydrogen when process gas is admitted to the reactor.
1. The mildly exothermic reactions are:
3 Fe2O3 + H2 ========= 2 Fe3O4 + H2O
3 Fe2O3 + CO ========= 2 Fe3O4 + CO2
BENFIELD LIQUOR:Determination of Diethanolamine Using an Auto TitratorGerard B. Hawkins
BENFIELD LIQUOR:Determination of Diethanolamine Using an Auto Titrator
1 SCOPE AND FIELD OF APPLICATION
This method is suitable for the determination of diethanolamine in Benfield Liquor.
2 PRINCIPLE
Diethanolamine is converted quantitatively into ammonia by boiling in the presence of sulfuric acid and copper sulfate. The ammonia is distilled from an alkaline medium and absorbed into boric acid. The solution is titrated with standard acid.
Determination of Residue on Evaporation in Anhydrous AmmoniaGerard B. Hawkins
Determination of Residue on Evaporation in Anhydrous Ammonia
1 SCOPE AND FIELD OF APPLICATION
This method is suitable for the determination of the residue left after evaporation i.e., the non-volatile material in ammonia solution.
2 PRINCIPLE
A known weight of sample is evaporated to dryness in a platinum dish on a steam bath. The increase in mass of the dish is measured.
Carbon Formation in Mixed Feed Preheat Coils:
Maximum Mixed Feed Pre-heat Temperature
What follows is a crude but effective routine, which evaluates the maximum possible temperature allowable to prevent excessive carbon laydown in the mixed feed pre-heat coils.
Determination of Hydrogen Sulfide by Cadmium Sulfide PrecipitationGerard B. Hawkins
Plant Analytical Techniques
Gas Analysis: Determination of Hydrogen Sulfide by Cadmium Sulfide Precipitation
SCOPE AND FIELD OF APPLICATION
This method is suitable for the in situ determination of hydrogen sulfide in ammonia plant gas streams when testing is required during catalyst reduction.
PRINCIPLE
Hydrogen sulfide present in the gas precipitates cadmium sulfide from a cadmium solution. The precipitate is filtered then reacted with iodine; the excess iodine is then titrated with sodium thiosulfate.
Physical properties and thermochemistry for reactor technologyGerard B. Hawkins
Physical Properties and Thermochemistry for Reactor Technology
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 PHYSICAL PROPERTIES
4.1 Form of Equations
4.2 The Physical Property System: “The VAULT”
4.3 Physical Property Programs
4.4 Physical Property Estimation
4.5 Sources of Expertise
5 INTERFACING COMPUTER PROGRAMS TO THE
GBHE VAULT PHYSICAL PROPERTIES PACKAGE
5.1 Preparation of the Physical Property Data
6 THERMOCHEMISTRY
6.1 Hess's Law
6.2 Standard States
6.3 Heats of Formation
6.4 Determination of Heats of Reaction
7 CALCULATION OF HEATS OF REACTION
7.1 Analogous Reactions
7.2 Heat of Formation Data Compilations
7.3 Estimation of Standard Heats of Formation
7.4 Heats of Neutralization
7.5 Temperature Effect on Heat of Reaction
8 HEATS OF SOLUTION, DILUTION AND MIXING
8.1 Calculation of Heats of Solution / Dilution from
Literature Data
8.2 Estimation of Heats of Solution and Mixing
8.3 Integral and Differential Heats
9 EXPERIMENTAL DETERMINATION OF
THERMOCHEMICAL PARAMETERS
9.1 Isoperibol Calorimetry for Heats of Reaction and Solution
9.2 Heat Flow Calorimetry
9.3 Adiabatic Calorimeter
9.4 Differential Scanning Calorimetry
10 COMPUTER CALCULATION OF ENTHALPY OR
TEMPERATURE
11 BIBLIOGRAPHY
Biological Systems: A Special Case
Up till now we have discussed various aspects of the separation and processing of fine solids without too much reference (except in the examples) to the specifics of the properties of the materials concerned. Though the material properties are the dominant influence on efficient process design and operation, it has been postulated that the necessary characteristics for process selection and optimization can be found fairly readily using easily-applicable rheological and other techniques. This underlying assumption also seems to hold good for biological suspensions; however, certain aspects of the behavior of these systems are sufficiently specialized for them to merit a separate discussion viz:
1 TYPES OF BIOLOGICAL SEPARATION
1.1 Whole-Organism Case
1.2 Part-Cell Separations
1.3 Isolation of Individual Molecular Species
2 SETTING ABOUT DEVISING AN EFFECTIVE
PROCESS FOR SEPARATION OF A BIOLOGICAL MATERIAL
2.1 Whole-Organism Case
2.1.1 Characterization of Biopolymers in the Liquor
2.1.2 Release of Internal Water
2.2 Part -Cell Separations
2.2.1 Selectivity
2.2.2 Cost
2.3 Isolation of Individual Molecular Species
3 Examples
3.1 Effective Design and Operation of a Process for Harvesting of Single Cell Protein
3.2 Harvesting of Mycoprotein for Human Consumption
3.3 Thickening of a Filamentous Organism Suspension
3.4 Separation of Poly-3-hydroxybutyrate Polymer (PHB) from Alcaligenes Eutrophus Biomass
3.5 Isolation of Organic Acid Produced by an Enzymatic Process
4 REFERENCES
Table
Figures
GE / Texaco Gasifier Feed to a Lurgi Methanol Plant and its Effect on Methano...Gerard B. Hawkins
GE / Texaco Gasifier Feed to a Lurgi Methanol Plant and its Effect on Methanol Production
CONTENTS
0 Methanol Synthesis Introduction
1 Executive Summary
2 Design Basis
2.1.1 Train I Design Basis
2.1.2 Train II Design Basis
2.1.3 Train III Design Basis
2.2 Design Philosophy
2.2.1 Operability Review
2.3 Assumptions
2.4 Train IV Flowsheet
2.4.1 CO2 Removal
3 Discussion
3.1 Natural Gas Consumption Figures
3.1.1 Base Case
3.1.2 Case 1 – Coal Gasification in Service
3.1.3 Case 2 – Coal Gasification in Service – No CO2 Export
3.2 Methanol Production Figures
3.2.1 Base Case
3.2.2 Case 1 – Coal Gasification in Service
3.2.3 Case 2 – Coal Gasification in Service – No CO2 Export
3.3 85% Natural Gas Availability
3.4 100% Natural Gas Availability
3.5 CO2 Emissions
3.5.1 Base Case
3.5.2 Case 1 – Coal Gasification in Service
3.5.3 Case 2 – Coal Gasification in Service – No CO2 Export
3.6 Specific Consumption Figures
3.6.1 Base Case
3.6.2 Case 1 – Coal Gasification and CO2 Import
3.6.3 Case 2 – Coal Gasification and No CO2 Import
3.7 Train IV Synthesis Gas Composition
4 Further Work
5 Conclusion
APPENDIX
Important Stream Data – Material Balance Stream Data
Texaco Gasifier with HP Steam Raising Boiler
CHARACTERISTICS OF COAL
Material Balance Considerations
High Temperature Shift Catalyst Reduction ProcedureGerard B. Hawkins
High Temperature Shift Catalyst Reduction Procedure
The catalyst, as supplied, is Fe2O3. This reduces to the active form, Fe3O4, in the presence of hydrogen when process gas is admitted to the reactor.
1. The mildly exothermic reactions are:
3 Fe2O3 + H2 ========= 2 Fe3O4 + H2O
3 Fe2O3 + CO ========= 2 Fe3O4 + CO2
BENFIELD LIQUOR:Determination of Diethanolamine Using an Auto TitratorGerard B. Hawkins
BENFIELD LIQUOR:Determination of Diethanolamine Using an Auto Titrator
1 SCOPE AND FIELD OF APPLICATION
This method is suitable for the determination of diethanolamine in Benfield Liquor.
2 PRINCIPLE
Diethanolamine is converted quantitatively into ammonia by boiling in the presence of sulfuric acid and copper sulfate. The ammonia is distilled from an alkaline medium and absorbed into boric acid. The solution is titrated with standard acid.
Determination of Residue on Evaporation in Anhydrous AmmoniaGerard B. Hawkins
Determination of Residue on Evaporation in Anhydrous Ammonia
1 SCOPE AND FIELD OF APPLICATION
This method is suitable for the determination of the residue left after evaporation i.e., the non-volatile material in ammonia solution.
2 PRINCIPLE
A known weight of sample is evaporated to dryness in a platinum dish on a steam bath. The increase in mass of the dish is measured.
Carbon Formation in Mixed Feed Preheat Coils:
Maximum Mixed Feed Pre-heat Temperature
What follows is a crude but effective routine, which evaluates the maximum possible temperature allowable to prevent excessive carbon laydown in the mixed feed pre-heat coils.
GBH Enterprises provides activated carbon regeneration services for refineries using a multi-step air-steam process. The process involves slowly depressurizing the carbon bed, applying steam to desorb contaminants, then introducing increments of air up to 5000 ppm to burn off remaining contaminants. Temperature and oxygen levels are monitored throughout to ensure safe regeneration of the activated carbon for reuse in purification processes.
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
This process duty specification refers to a Syngas Conditioning Unit which utilizes HT Shift reaction technology on a slip stream of raw gas to produce a recombined gas stream with a H2:CO ratio of 1.57:1. This is an important consideration as the Shift reactor is not required to minimize CO at outlet, and this specification refers to the expected performance that can be achieved in a single stage reactor scheme.
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.
Reactor Arrangement for Continuous Vapor Phase ChlorinationGerard B. Hawkins
Reactor Arrangement for Continuous Vapor Phase Chlorination
CONTENTS
1 BACKGROUND
2 REACTOR
3 CHEMICAL SYSTEM
4 PROCESS CHEMISTRY
5 KINETICS EXPERIMENTS AND MODELING
6 INTERPRETATION OF KINETICS INFORMATION
7 OPERATING CONDITIONS AND REACTOR DESIGN
8 REACTOR STABILITY AND CONTROL
FIGURES
1 POSTULATED REACTION PATHS FOR PROGRESSIVE CHLORINATION OF B-PICOLINE 3
2 CHLORINATION OF b-PICOLINE: MODEL PREDICTIONS OF PRODUCT DISTRIBUTION IN FULLY-MIXED REACTOR
3 TWO-STAGE REACTOR: RATE OF CHLORINATION OF b-PICOLINE
DOCUMENTS REFERRED TO IN THIS PROCESS ENGINEERING GUIDE
Fixed Bed Reactor Scale-up Checklist
The purpose of this checklist is to identify the stages and potential problems associated with the scale up of fixed bed reactors from the drawing board to the full scale plant, and to determine how they should be checked.
The checking can be done using various methods. These are:
• Literature data.
• Lab testing.
• Calculation.
• Modeling.
• Semi-tech testing.
• Piloting or Sidestream testing.
Identifying the stages that need to be addressed for a particular catalyst/reactor development will help in estimating the time needed for the development of the reactor
Determination of Residue and Oil in Anhydrous AmmoniaGerard B. Hawkins
Plant Analytical Techniques
Determination of Residue and Oil in Anhydrous Ammonia
This method is suitable for the determination of residue and oil in anhydrous ammonia.
FIELD OF APPLICATION
This method may be applied to standard and premium grade anhydrous ammonia having residue content in the range 10-5000 micrograms per gram and oil content in the range l-500 micrograms per gram
Catalyst poisons & fouling mechanisms the impact on catalyst performance Gerard B. Hawkins
Primary Effects
Secondary Effects
Typical Poisons in hydrocarbon processing
Permanent Poisons
- Arsenic, lead, mercury, cadmium…
- Silica, Iron Oxide….
Temporary Poisons
- Sulfur, Chlorides, Carbon
Boiler Feed water impurities
Heavy Metals
Foulants
THE NATURE OF CARBON DEPOSITS FORMED ON CATALYSTS
- CARBON FORMATION
Type A, B, C
- FEEDSTOCK COMPOSITION EFFECTS
COMMERCIAL’ CARBON DEPOSITS
- CARBON BURNING IN AIR
- CARBON REMOVAL BY STEAMING
- CARBON BURN CONTROL METHODS
- CATALYST – REACTION WITH STEAM
- MAXIMUM OXYGEN CONCENTRATION
- TEMPERATURE OF THE CATALYST SURFACE DURING CARBON BURNS
- CONDITIONS TO BURN OFF CARBON COATED CATALYST
- EFFECT OF CARBON FORMATION
Determination of Oxygen in Anhydrous Ammonia
SCOPE AND FIELD OF APPLICATION
This method is suitable for the determination of trace amounts of oxygen in Liquefied anhydrous ammonia.
The trace oxygen analyzer provides for trace oxygen analysis in decade steps ranging from 0 - 10 to 0 - 10,000 ppm v/v (full scale).
Investigation of the Potential Use of (IILs) Immobilized Ionic Liquids in Sha...Gerard B. Hawkins
The document discusses using immobilized ionic liquids (IILs) in shale gas sweetening reactions. It proposes immobilizing a cobalt catalyst in the surface ionic liquid layer of a solid supported ionic liquid catalyst. This would create a "homogeneous catalyst" dissolved within the fixed IIL layer. Competing reactions like oxidation of sulfides to sulfones would need to be considered. Related work on using similar approaches for hydroformylation reactions is referenced. The concept aims to develop a solid IIL catalyst for sweetening reactions involving oxidation using techniques from other areas like hydroformylation.
The Selection of Flocculants and other Solid-Liquid Separation AidsGerard B. Hawkins
The use of chemical additives, such as flocculants, is a common step in solid-liquid separation operations. The correct selection of agent is an essential part of the design of such processes. Many excellent reviews and guides deal with this topic, and the interested reader is referred to works such as [l-4]. In particular the Harwell-Warren Spring Report “The Use and Selection of Flocculants" provides a good overview on the application of coagulants and flocculants. This section does not attempt to reproduce a detailed treatment of that kind; instead it is our intention to state a few general rules and principles concerning methods of choosing an additive, and to illustrate briefly their application in practice.
The types of agents employed in solid-liquid separation fall into three principal classes:
DEACTIVATION OF METHANOL SYNTHESIS CATALYSTS
CONTENTS
1 INTRODUCTION
2 THERMAL SINTERING
3 CATALYST POISONING
4 REACTANT INDUCED DEACTIVATION
5 SUMMARY
TABLES
1 DEACTIVATION PROCESSES ON METHANOL SYNTHESIS CATALYSTS
2 MELTING POINT, HUTTIG AND TAMMANN TEMPERATURES OF COPPER, IRON AND NICKEL
3 SINTERING RATE CONSTANTS CALCULATED INLET AND OUTLET SIDE STREAM UNIT FOR VULCAN VSG-M101
4 COMPARISON BETWEEN CALCULATED S∞ AND DISCHARGED MEASUREMENTS ON VULCAN VSG-M101
5 EFFECT OF POSSIBLE CONTAMINANTS AND POISONS ON CU/ZNO/AL2O3 CATALYSTS FOR METHANOL SYNTHESIS
6 GUARD SCREENING TEST RESULTS ON METHANOL MICRO-REACTOR. EFFECT OF DEPOSITED METALS ON METHANOL ACTIVITY
FIGURES
1 THE HΫTTIG AND TAMMANN TEMPERATURES OF THE COMPONENTS OF A SYNTHESIS CATALYST
2 A SCHEMATIC REPRESENTATION OF TWO CATALYST SINTERING MECHANISMS
3 SIDE STREAM DATA FOR VULCAN VSG-M101. INLET TEMPERATURE 242 OC, PRESSURE 1500 PSI, GAS COMPOSITION 6% CO, 9.2% CO2, 66.9% H2, 2.5% N2 AND 15.4% CH4, SPACE VELOCITY 17,778 HR-1. MEAN OUTLET TEMPERATURE 280 OC
4 TEMPERATURE DEPENDENCE OF THE RATE OF SINTERING
5 MECHANISM OF SULFUR RETENTION
6 CORRELATION OF SULFUR CAPACITY WITH TOTAL SURFACE AREA
7 EFFECT OF DEPOSITED (NI+FE) PPM ON METHANOL SYNTHESIS CATALYST ACTIVITY
8 DISCHARGED (FE + NI) DEPOSITION LEVELS ON METHANOL SYNTHESIS PLANT SAMPLES
9 EPMA ANALYSIS OF DISCHARGED LABORATORY SAMPLE OF POISONED VULCAN VSG-M101
10 THE EFFECT OF CO2 ON SYNTHESIS CATALYST DEACTIVATION
REFERENCES
The document describes STANJAN, an interactive program for chemical equilibrium analysis using the element potential method. STANJAN can solve problems involving multiple phases and complex species. It assumes ideal gas and ideal solution models. Examples shown include a carbon-rich CO system, a fiber optics manufacturing system with two phases, and calculating adiabatic flame temperature and nozzle exit conditions for a gas turbine combustor reaction. STANJAN provides a robust, user-friendly way to analyze chemical equilibria in various applications.
Filtration
0 INTRODUCTION
1 The Theory Underlying Filtration Processes
1.1 The Mechanism of Simple Filtration Systems
1.1.2 Cake Filtration
1.1.3 Complete Blocking
1.1.4 Standard Blocking
1.1.5 Intermediate Blocking
1.2 Cake Filtration – Models and Mechanisms
1.2.1 Classical Theory for the Permeability of Porous Cakes and Beds
1.2.2 The Rate of Filtration through a Compressible Cake – The Standard Filtration Equation
1.2.3 The Compression or Consolidation of Filter Cakes – Ultimate degree of dewatering
1.2.4 The Rate of Consolidation
1.2.5 Useful Semi-Empirical Relations for Constant Pressure and Constant Rate Cake Filtration
1.2.6 Constant Pressure Filtration
1.2.7 Constant Rate Filtration
1.2.8 Multiphase Theory of Filtration
1.3 Crossflow Filtration
2 The Range and Selection of Filtration Equipment Technology
2.1 Scale
2.2 Solids Recovery, Liquids Clarification or Feed stream Concentration
2.3 Rate of Sedimentation
2.4 Rate of Cake Formation and Drainage
2.5 Batch vs Continuous Operation
2.6 Solids Loading
2.7 Further Processing
2.8 Aseptic or “Hygienic” Operation
2.9 Miscellaneous
2.10 Shear versus Compressional Deformation
2.11 Pressure versus Vacuum
3 Suspension Conditioning Prior to Filtration
3.1 Simple Filtration Aids
3.2 Mechanical Treatments
4 Post-Filtration Treatments and Further Downstream Processing
4.1 Washing
4.1.1 Air-Blowing
4.1.2 Drying
5 Testing and Characterization of Suspensions
5.1 Introduction – Suspension
5.2 Properties relevant to Filtration Performance
5.2.1 Pre-Filtration Properties of Suspension
5.2.2 Properties of Filter Cake
5.2.3 Laboratory Scale Filtration Rigs
5.3 Means of Monitoring Flocculant Dosage
5.4 Filter Cake Testing
5.4.1 Strength Testing (See also piston press described earlier)
5.4.2 Cake Permeability or Resistance
5.4.3 Rate of Cake Formation
6 Examples of the Application of the Forgoing Principles
6.1 Dewatering of Calcium Carbonate Slurries
6.2 Dewatering of Organic Products – Procion Dyestuffs
6.3 Filtration of Biological Systems – Harvesting a Filamentous Organism
References
Tables
Figures
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
Determination of Anions by Ion Chromatography
1 SCOPE AND FIELD OF APPLICATION
This method is suitable for the determination of inorganic anions in Ammonia Solution in the range 100 ppb to 50 ppm m/v.
2 PRINCIPLE
The sample is passed through a column of anion exchange resin, on which the anions are absorbed and separated. They are then eluted with dilute sodium carbonate/sodium hydrogen carbonate solution and passed through a suppressor. This replaces the cations with hydrogen ions and thus reduces the background conductivity of the eluent. Final measurement is by conductivity
"SEDIMENTATION"
INTRODUCTION - THE PHENOMENON OF SEDIMENTATION
Sedimentation is the physical process whereby solid particles, of greater density than their suspending medium, will tend to separate into regions of higher concentration under the influence of gravity. As a solids/liquids separation technique it therefore possesses the great advantage of utilizing a natural, and therefore costless, driving force. This section of the suspension processing Guide is Intended to provide an Introduction to the science of the subject, and the means to judge where and how best to exploit sedimentation as a separation (or other processing) technique.
As a scientific discipline the subject of sedimentation is vast with perspectives ranging from the field of chemical engineering through to theoretical physics being covered In the literature [1-11]. Good reviews of the subject, with a bias towards the engineering aspects, have been written by Fitch and Koz [12, 13]. A short summary of some of the more relevant contributions from the literature is also provided in GBHE-SPG-PEG-302 “Basic Principles & Test Methods”, of the Suspensions Processing Guides.
.
The sedimentation process is traditionally divided into ..."
Chemical Process Conception
0 INTRODUCTION / PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 PRODUCT STRATEGY
4.1 General
4.2 Market for the Product
4.3 Production Costs
4.4 Process Technology
5 PRELIMINARY PROCESS INFORMATION
6 REACTION AND REACTOR
6.1 Batch vs Continuous
6.2 Multiple Reactors
7 RECYCLE
7.1 Recycle Structure
7.2 Classification of Chemicals
7.3 Effect of Recycle
7.4 Preliminary Estimation of Conversion
8 REACTOR TYPE AND PERFORMANCE
8.1 Conversion-Yield Effects
8.2 Heat Effects
8.3 Equilibrium Effects
8.4 Kinetic Effects
8.5 More Help with Reactor Design
9 SEPARATION SYSTEM
10 REVIEW
11 BIBLIOGRAPHY AND REFERENCES
11.1 Preliminary Flowsheeting
11.2 Physical Properties
11.3 Reactors
11.4 Separation
11.5 Costing
APPENDICES
A BASIC REACTOR SYSTEM DESIGN
B DISCUSSION BETWEEN A CHEMIST AND A
CHEMICAL ENGINEER
C BASIC SEPARATION STRATEGY
TABLES
1 CLASSIFICATION OF MATERIALS
FIGURES
1 FLOWCHART OF THE ITERATIVE PROCEDURE REQUIRED IN PROCESS AND PRODUCT SELECTION AND DEVELOPMENT
Low Temperature Shift Catalyst Reduction Procedure
VSG-C111 as supplied contains copper oxide; it is activated for the low temperature shift duty by reducing the copper oxide component to metallic copper with hydrogen. The reaction is highly exothermic. In order to achieve maximum activity, good performance and long life, it is essential that the reduction is conducted under correctly controlled conditions. Great care must be taken to avoid thermal damage during this critical operation.
In-Situ Oxidation Procedure for High and Low Temperature Shift CatalystsGerard B. Hawkins
GBH Enterprises provides a 7-step procedure for the in-situ oxidation of high and low temperature shift catalysts prior to removal from the system. The procedure involves purging combustibles, cooling the catalyst beds, metering in air at increasing rates, and monitoring temperatures until oxidation is complete, estimated at 12 hours. The process allows for the controlled oxidation and safe discharge of the catalysts.
GBH Enterprises provides activated carbon regeneration services for refineries using a multi-step air-steam process. The process involves slowly depressurizing the carbon bed, applying steam to desorb contaminants, then introducing increments of air up to 5000 ppm to burn off remaining contaminants. Temperature and oxygen levels are monitored throughout to ensure safe regeneration of the activated carbon for reuse in purification processes.
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
This process duty specification refers to a Syngas Conditioning Unit which utilizes HT Shift reaction technology on a slip stream of raw gas to produce a recombined gas stream with a H2:CO ratio of 1.57:1. This is an important consideration as the Shift reactor is not required to minimize CO at outlet, and this specification refers to the expected performance that can be achieved in a single stage reactor scheme.
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.
Reactor Arrangement for Continuous Vapor Phase ChlorinationGerard B. Hawkins
Reactor Arrangement for Continuous Vapor Phase Chlorination
CONTENTS
1 BACKGROUND
2 REACTOR
3 CHEMICAL SYSTEM
4 PROCESS CHEMISTRY
5 KINETICS EXPERIMENTS AND MODELING
6 INTERPRETATION OF KINETICS INFORMATION
7 OPERATING CONDITIONS AND REACTOR DESIGN
8 REACTOR STABILITY AND CONTROL
FIGURES
1 POSTULATED REACTION PATHS FOR PROGRESSIVE CHLORINATION OF B-PICOLINE 3
2 CHLORINATION OF b-PICOLINE: MODEL PREDICTIONS OF PRODUCT DISTRIBUTION IN FULLY-MIXED REACTOR
3 TWO-STAGE REACTOR: RATE OF CHLORINATION OF b-PICOLINE
DOCUMENTS REFERRED TO IN THIS PROCESS ENGINEERING GUIDE
Fixed Bed Reactor Scale-up Checklist
The purpose of this checklist is to identify the stages and potential problems associated with the scale up of fixed bed reactors from the drawing board to the full scale plant, and to determine how they should be checked.
The checking can be done using various methods. These are:
• Literature data.
• Lab testing.
• Calculation.
• Modeling.
• Semi-tech testing.
• Piloting or Sidestream testing.
Identifying the stages that need to be addressed for a particular catalyst/reactor development will help in estimating the time needed for the development of the reactor
Determination of Residue and Oil in Anhydrous AmmoniaGerard B. Hawkins
Plant Analytical Techniques
Determination of Residue and Oil in Anhydrous Ammonia
This method is suitable for the determination of residue and oil in anhydrous ammonia.
FIELD OF APPLICATION
This method may be applied to standard and premium grade anhydrous ammonia having residue content in the range 10-5000 micrograms per gram and oil content in the range l-500 micrograms per gram
Catalyst poisons & fouling mechanisms the impact on catalyst performance Gerard B. Hawkins
Primary Effects
Secondary Effects
Typical Poisons in hydrocarbon processing
Permanent Poisons
- Arsenic, lead, mercury, cadmium…
- Silica, Iron Oxide….
Temporary Poisons
- Sulfur, Chlorides, Carbon
Boiler Feed water impurities
Heavy Metals
Foulants
THE NATURE OF CARBON DEPOSITS FORMED ON CATALYSTS
- CARBON FORMATION
Type A, B, C
- FEEDSTOCK COMPOSITION EFFECTS
COMMERCIAL’ CARBON DEPOSITS
- CARBON BURNING IN AIR
- CARBON REMOVAL BY STEAMING
- CARBON BURN CONTROL METHODS
- CATALYST – REACTION WITH STEAM
- MAXIMUM OXYGEN CONCENTRATION
- TEMPERATURE OF THE CATALYST SURFACE DURING CARBON BURNS
- CONDITIONS TO BURN OFF CARBON COATED CATALYST
- EFFECT OF CARBON FORMATION
Determination of Oxygen in Anhydrous Ammonia
SCOPE AND FIELD OF APPLICATION
This method is suitable for the determination of trace amounts of oxygen in Liquefied anhydrous ammonia.
The trace oxygen analyzer provides for trace oxygen analysis in decade steps ranging from 0 - 10 to 0 - 10,000 ppm v/v (full scale).
Investigation of the Potential Use of (IILs) Immobilized Ionic Liquids in Sha...Gerard B. Hawkins
The document discusses using immobilized ionic liquids (IILs) in shale gas sweetening reactions. It proposes immobilizing a cobalt catalyst in the surface ionic liquid layer of a solid supported ionic liquid catalyst. This would create a "homogeneous catalyst" dissolved within the fixed IIL layer. Competing reactions like oxidation of sulfides to sulfones would need to be considered. Related work on using similar approaches for hydroformylation reactions is referenced. The concept aims to develop a solid IIL catalyst for sweetening reactions involving oxidation using techniques from other areas like hydroformylation.
The Selection of Flocculants and other Solid-Liquid Separation AidsGerard B. Hawkins
The use of chemical additives, such as flocculants, is a common step in solid-liquid separation operations. The correct selection of agent is an essential part of the design of such processes. Many excellent reviews and guides deal with this topic, and the interested reader is referred to works such as [l-4]. In particular the Harwell-Warren Spring Report “The Use and Selection of Flocculants" provides a good overview on the application of coagulants and flocculants. This section does not attempt to reproduce a detailed treatment of that kind; instead it is our intention to state a few general rules and principles concerning methods of choosing an additive, and to illustrate briefly their application in practice.
The types of agents employed in solid-liquid separation fall into three principal classes:
DEACTIVATION OF METHANOL SYNTHESIS CATALYSTS
CONTENTS
1 INTRODUCTION
2 THERMAL SINTERING
3 CATALYST POISONING
4 REACTANT INDUCED DEACTIVATION
5 SUMMARY
TABLES
1 DEACTIVATION PROCESSES ON METHANOL SYNTHESIS CATALYSTS
2 MELTING POINT, HUTTIG AND TAMMANN TEMPERATURES OF COPPER, IRON AND NICKEL
3 SINTERING RATE CONSTANTS CALCULATED INLET AND OUTLET SIDE STREAM UNIT FOR VULCAN VSG-M101
4 COMPARISON BETWEEN CALCULATED S∞ AND DISCHARGED MEASUREMENTS ON VULCAN VSG-M101
5 EFFECT OF POSSIBLE CONTAMINANTS AND POISONS ON CU/ZNO/AL2O3 CATALYSTS FOR METHANOL SYNTHESIS
6 GUARD SCREENING TEST RESULTS ON METHANOL MICRO-REACTOR. EFFECT OF DEPOSITED METALS ON METHANOL ACTIVITY
FIGURES
1 THE HΫTTIG AND TAMMANN TEMPERATURES OF THE COMPONENTS OF A SYNTHESIS CATALYST
2 A SCHEMATIC REPRESENTATION OF TWO CATALYST SINTERING MECHANISMS
3 SIDE STREAM DATA FOR VULCAN VSG-M101. INLET TEMPERATURE 242 OC, PRESSURE 1500 PSI, GAS COMPOSITION 6% CO, 9.2% CO2, 66.9% H2, 2.5% N2 AND 15.4% CH4, SPACE VELOCITY 17,778 HR-1. MEAN OUTLET TEMPERATURE 280 OC
4 TEMPERATURE DEPENDENCE OF THE RATE OF SINTERING
5 MECHANISM OF SULFUR RETENTION
6 CORRELATION OF SULFUR CAPACITY WITH TOTAL SURFACE AREA
7 EFFECT OF DEPOSITED (NI+FE) PPM ON METHANOL SYNTHESIS CATALYST ACTIVITY
8 DISCHARGED (FE + NI) DEPOSITION LEVELS ON METHANOL SYNTHESIS PLANT SAMPLES
9 EPMA ANALYSIS OF DISCHARGED LABORATORY SAMPLE OF POISONED VULCAN VSG-M101
10 THE EFFECT OF CO2 ON SYNTHESIS CATALYST DEACTIVATION
REFERENCES
The document describes STANJAN, an interactive program for chemical equilibrium analysis using the element potential method. STANJAN can solve problems involving multiple phases and complex species. It assumes ideal gas and ideal solution models. Examples shown include a carbon-rich CO system, a fiber optics manufacturing system with two phases, and calculating adiabatic flame temperature and nozzle exit conditions for a gas turbine combustor reaction. STANJAN provides a robust, user-friendly way to analyze chemical equilibria in various applications.
Filtration
0 INTRODUCTION
1 The Theory Underlying Filtration Processes
1.1 The Mechanism of Simple Filtration Systems
1.1.2 Cake Filtration
1.1.3 Complete Blocking
1.1.4 Standard Blocking
1.1.5 Intermediate Blocking
1.2 Cake Filtration – Models and Mechanisms
1.2.1 Classical Theory for the Permeability of Porous Cakes and Beds
1.2.2 The Rate of Filtration through a Compressible Cake – The Standard Filtration Equation
1.2.3 The Compression or Consolidation of Filter Cakes – Ultimate degree of dewatering
1.2.4 The Rate of Consolidation
1.2.5 Useful Semi-Empirical Relations for Constant Pressure and Constant Rate Cake Filtration
1.2.6 Constant Pressure Filtration
1.2.7 Constant Rate Filtration
1.2.8 Multiphase Theory of Filtration
1.3 Crossflow Filtration
2 The Range and Selection of Filtration Equipment Technology
2.1 Scale
2.2 Solids Recovery, Liquids Clarification or Feed stream Concentration
2.3 Rate of Sedimentation
2.4 Rate of Cake Formation and Drainage
2.5 Batch vs Continuous Operation
2.6 Solids Loading
2.7 Further Processing
2.8 Aseptic or “Hygienic” Operation
2.9 Miscellaneous
2.10 Shear versus Compressional Deformation
2.11 Pressure versus Vacuum
3 Suspension Conditioning Prior to Filtration
3.1 Simple Filtration Aids
3.2 Mechanical Treatments
4 Post-Filtration Treatments and Further Downstream Processing
4.1 Washing
4.1.1 Air-Blowing
4.1.2 Drying
5 Testing and Characterization of Suspensions
5.1 Introduction – Suspension
5.2 Properties relevant to Filtration Performance
5.2.1 Pre-Filtration Properties of Suspension
5.2.2 Properties of Filter Cake
5.2.3 Laboratory Scale Filtration Rigs
5.3 Means of Monitoring Flocculant Dosage
5.4 Filter Cake Testing
5.4.1 Strength Testing (See also piston press described earlier)
5.4.2 Cake Permeability or Resistance
5.4.3 Rate of Cake Formation
6 Examples of the Application of the Forgoing Principles
6.1 Dewatering of Calcium Carbonate Slurries
6.2 Dewatering of Organic Products – Procion Dyestuffs
6.3 Filtration of Biological Systems – Harvesting a Filamentous Organism
References
Tables
Figures
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
Determination of Anions by Ion Chromatography
1 SCOPE AND FIELD OF APPLICATION
This method is suitable for the determination of inorganic anions in Ammonia Solution in the range 100 ppb to 50 ppm m/v.
2 PRINCIPLE
The sample is passed through a column of anion exchange resin, on which the anions are absorbed and separated. They are then eluted with dilute sodium carbonate/sodium hydrogen carbonate solution and passed through a suppressor. This replaces the cations with hydrogen ions and thus reduces the background conductivity of the eluent. Final measurement is by conductivity
"SEDIMENTATION"
INTRODUCTION - THE PHENOMENON OF SEDIMENTATION
Sedimentation is the physical process whereby solid particles, of greater density than their suspending medium, will tend to separate into regions of higher concentration under the influence of gravity. As a solids/liquids separation technique it therefore possesses the great advantage of utilizing a natural, and therefore costless, driving force. This section of the suspension processing Guide is Intended to provide an Introduction to the science of the subject, and the means to judge where and how best to exploit sedimentation as a separation (or other processing) technique.
As a scientific discipline the subject of sedimentation is vast with perspectives ranging from the field of chemical engineering through to theoretical physics being covered In the literature [1-11]. Good reviews of the subject, with a bias towards the engineering aspects, have been written by Fitch and Koz [12, 13]. A short summary of some of the more relevant contributions from the literature is also provided in GBHE-SPG-PEG-302 “Basic Principles & Test Methods”, of the Suspensions Processing Guides.
.
The sedimentation process is traditionally divided into ..."
Chemical Process Conception
0 INTRODUCTION / PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 PRODUCT STRATEGY
4.1 General
4.2 Market for the Product
4.3 Production Costs
4.4 Process Technology
5 PRELIMINARY PROCESS INFORMATION
6 REACTION AND REACTOR
6.1 Batch vs Continuous
6.2 Multiple Reactors
7 RECYCLE
7.1 Recycle Structure
7.2 Classification of Chemicals
7.3 Effect of Recycle
7.4 Preliminary Estimation of Conversion
8 REACTOR TYPE AND PERFORMANCE
8.1 Conversion-Yield Effects
8.2 Heat Effects
8.3 Equilibrium Effects
8.4 Kinetic Effects
8.5 More Help with Reactor Design
9 SEPARATION SYSTEM
10 REVIEW
11 BIBLIOGRAPHY AND REFERENCES
11.1 Preliminary Flowsheeting
11.2 Physical Properties
11.3 Reactors
11.4 Separation
11.5 Costing
APPENDICES
A BASIC REACTOR SYSTEM DESIGN
B DISCUSSION BETWEEN A CHEMIST AND A
CHEMICAL ENGINEER
C BASIC SEPARATION STRATEGY
TABLES
1 CLASSIFICATION OF MATERIALS
FIGURES
1 FLOWCHART OF THE ITERATIVE PROCEDURE REQUIRED IN PROCESS AND PRODUCT SELECTION AND DEVELOPMENT
Low Temperature Shift Catalyst Reduction Procedure
VSG-C111 as supplied contains copper oxide; it is activated for the low temperature shift duty by reducing the copper oxide component to metallic copper with hydrogen. The reaction is highly exothermic. In order to achieve maximum activity, good performance and long life, it is essential that the reduction is conducted under correctly controlled conditions. Great care must be taken to avoid thermal damage during this critical operation.
In-Situ Oxidation Procedure for High and Low Temperature Shift CatalystsGerard B. Hawkins
GBH Enterprises provides a 7-step procedure for the in-situ oxidation of high and low temperature shift catalysts prior to removal from the system. The procedure involves purging combustibles, cooling the catalyst beds, metering in air at increasing rates, and monitoring temperatures until oxidation is complete, estimated at 12 hours. The process allows for the controlled oxidation and safe discharge of the catalysts.
Other Separations Techniques for Suspensions
PRESSURE-DRIVEN MEMBRANE SEPARATION
PROCESSES
1.1 INTRODUCTION
1.2 MEMBRANES
1.3 OPERATION
1.4 FACTORS AFFECTING PERFORMANCE
1.4.1 Polarization / Fouling
1.4.2 Pressure
1.4.3 Crossflow
1.4.4 Temperature
1.4.5 Concentration
1.4.6 Membrane Pore Size
1.4.7 Particle Size
1.4.8 Particle Charge
1.4.9 Other Factors
1.5 ADVANTAGES / LIMITATIONS
1.6 SUMMARY OF SYMBOLS USED
2 ELECTRO-DIALYSIS
2.1 INTRODUCTION
2.2 EQUIPMENT
2.3 IMPORTANT PARAMETERS IN ED
2.4 EXAMPLES
3 ELECTRODEWATERING AND ELECTRODECANTATION
3.1 INTRODUCTION
3.2 PRINCIPLES AND OPERATION
3.3 EQUIPMENT AND OPERATING PARAMETERS
3.4 EXAMPLES
4 MAGNETIC SEPARATION METHODS
5 REFERENCES
FIGURES
1 APPLICATION RANGES FOR MEMBRANE SEPARATION TECHNIQUES
2 SIMPLE UF / CMF RIG
4 FLUX VERSUS PRESSURE
5 ELECTRODIALYSIS PROCESS
6 ELECTRODIALYSIS PLANT FOR BATCH PROCESS
7 DEPENDENCE OF MEMBRANE AREA AND ENERGY ON
CURRENT DENSITY
8 DIFFUSION ACROSS THE BOUNDARY LAYER
Determination of Argon in Ammonia Plant Process Gas Streams by Gas Chromatogr...Gerard B. Hawkins
Determination of Argon in Ammonia Plant Process Gas Streams by Gas Chromatography
SCOPE AND FIELD OF APPLICATION
This document is a method for the determination of argon in process gas streams in the range 0-10% v/v.
Reactor Modeling Tools – Multiple Regressions
CONTENTS
0 INTRODUCTION
1 SCOPE
2 THEORY
3 EXCEL 2007: MULTIPLE REGRESSIONS
3.1 Overview
3.2 Multiple Regression Using the Data Analysis ADD-IN
3.3 Interpret Regression Statistics Table
3.4 Interpret ANOVA Table
3.5 Interpret Regression Coefficients Table
3.6 Confidence Intervals for Slope Coefficients
3.7 Test Hypothesis of Zero Slope Coefficients ("Test of Statistical Significance")
3.8 Test Hypothesis on a Regression Parameter
3.8.1 Using the p-value approach
3.8.2 Using the critical value approach
3.9 Overall Test of Significance of the Regression Parameters
3.10 Predicted Value of Y Given Regressors
3.11 Excel Limitations
4 SPECIAL FEATURES REQUIRING MORE SOPHISTICATED TECHNIQUES
5 USER INFORMATION SUPPLIED
A SUBROUTINE
B DATA
C RESULTS
6 EXAMPLE
0 INTRODUCTION
The four main sources of Fugitive Emissions on most plants are valves, machine seals, re-makable joints and pressure relief devices. Other possible sources include open-ended lines, sampling connections, drains and vents.
Sometimes special precautions are taken to minimize Fugitive Emissions, for example the use of bellows seal valves. However, generally no special precautions are taken and the subsequent Fugitive Emissions to atmosphere represent a significant amount of plant losses.
Regulatory requirements covering Fugitive Emissions exist in many countries and therefore a leak reduction program should be implemented. Fugitive Emissions also represent financial losses to the business as well as potential damage to the environment.
Determination of Carbon Dioxide, Ethane And Nitrogen in Natural Gas by Gas C...Gerard B. Hawkins
Determination of Carbon Dioxide, Ethane
And Nitrogen in Natural Gas by Gas Chromatography
1 SCOPE AND FIELD OF APPLICATION
This document is a method for the determination of carbon dioxide, ethane and nitrogen in natural gas in the range 0-10% v/v.
2 PRINCIPLE
The gas sample will be injected automatically by a ten port valve onto the poraplot U column. The nitrogen will elute first and be switched to the mole sieve column. The mole sieve column will be isolated and the poraplot column will elute the carbon dioxide and ethane via a restrictor column to the detector. After the elution of the carbon dioxide and ethane the poraplot column will be back flushed. Then the nitrogen will be allowed to elute from the mole sieve column (see figure 1.) ...
Process Synthesis
INTRODUCTION
1 A SUGGESTED GENERAL APPROACH
2 EXAMPLES OF PROCESS SELECTION
2.1 Harvesting and Thickening of Single Cell Protein
2.2 Dewatering of a Specialty Latex
3 REFERENCES
TABLES
1 THE ADVANTAGES AND DISADVANTAGES OF DIFFERENT RANGE OF PH FOR “PROTEIN” ORGANISM FLOCCULATION
2 THE ADVANTAGES AND DISADVANTAGES OF VARYING EXTENTS OF CELL BREAKAGES
3 PREDICTED AND OBSERVED FILTER CAKE SOLIDS CONTENTS FOR THE VARIOUS LATICES AFTER COAGULATION
FIGURES
1 THE “PROTEIN” BACTERIAL HARVESTING SYSTEM
2 PROCESS FOR MANUFACTURE OF CALCIUM CARBONATE FILTERS
3 H-ACID ISOLATION
4 A SUGGESTED APPROACH TO DETERMINING FEASIBLE PROCESS OPTIONS, AND OPERATING CONDITIONS FOR SEPARATION OF FINE SOLIDS FROM SUSPENSION
5 MODULI VERSUS SOLIDS CONTENT FORTYPICAL FORWARD FLOCCULATED “PROTEIN” SUSPENSIONS
6 DECISION TREE FOR SELECTION OF AS1 HARVESTING CONDITIONS WHEN PRINCIPAL CONSTRAINT CONCERNS THE DEGREE OF THICKENING REQUIRED IN THE CONCENTRATE
7 DECISION TREE FOR SELECTION OF AS1 HARVESTING CONDITIONS WHEN PRINCIPAL CONSTRAINT CONCERNS THE USE OF FLOTATION AS A UNIT OPERATION FOR THICKENING
8 DECISION TREE FOR SELECTION OF AS1 HARVESTING CONDITIONS WHEN PRINCIPAL CONSTRAINT CONCERNS THE QUALITY OF THE RECYCLED LIQUOR
9 MODULUS SOLIDS CONTENT CURVES FOR THEVARIOUS COAGULATED LATICES
Determination of Hydrocarbons in Anhydrous Ammonia By Gas ChromatographyGerard B. Hawkins
Determination of Hydrocarbons in Anhydrous Ammonia By Gas Chromatography
SCOPE AND FIELD OF APPLICATION
The method is suitable for the determination of hydrocarbons from C1 to C4 (see 6.4.2) in gaseous ammonia, or in mixtures of ammonia and air. It is valid for concentrations in the range 10-10000 ppm.
The method may be used for the analysis of the atmosphere from a ships hold After purging with ammonia and for the analysis of gasified liquid anhydrous ammonia during or after loading. In these cases, hydrocarbon contamination may arise from the previous cargo of the vessel, the nature of which should be ascertained prior to carrying out the analysis
Integration of Special Purpose Centrifugal Pumps into a ProcessGerard B. Hawkins
Integration of Special Purpose Centrifugal Pumps into a Process
CONTENTS
1 SCOPE
2 PRELIMINARY CHOICE OF PUMP
SECTION A - INLET CONDITIONS
Al Calculation of Basic Nett Positive Suction Head (NPSH)
A2 Correction to Basic NPSH for Temperature Rise at Pump Inlet
A3 Correction to Basic NPSH for Acceleration Head
A4 Calculation of Available NPSH
A5 Correction to NPSH for Fluid Properties
A6 Calculation of Suction Specific Speed
A7 Priming
A8 Submergence
SECTION B – FLOW / HEAD RATING SEQUENCE
B1 Calculation of Static Head
B2 Calculation of Margins for Control
B3 Calculation of Q-H Duty
B4 Stability and Parallel Operation
B5 Corrections to Q-H Duty for Fluid Properties
B6 Guide to Pump Type and Speed
SECTION C – DRIVER POWER RATING
C1 Estimation of Pump Efficiency
C2 Calculation of Absorbed Power
C3 Calculation of Driver Power Rating
C4 Preliminary Power Ratings of Electric Motors
C5 Starting Conditions for Electric Motors
C6 Reverse Flow and Reverse Rotation
SECTION D - CASING PRESSURE RATING
D1 Calculation of Maximum Inlet Pressure
D2 Calculation of Differential Pressure
D3 Pressure Waves
D4 Pressure due to Liquid Thermal Expansion
D5 Casing Hydrostatic Test Pressure
SECTION E – SEALING CONSIDERATIONS
E1 Preliminary Choice of Seal
E2 Fluid Attributes
E3 Definition of Flushing Arrangements
APPENDICES
A RELIABILITY CLASSIFICATION
B SYMBOLS AND PREFERRED UNITS
DOCUMENTS REFERRED TO IN THIS ENGINEERING DESIGN GUIDE
GBH Enterprises specializes in catalyst and process technology for refining, gas processing, and petrochemical industries. They provide catalyst performance evaluation, heat and mass balance analysis, and commercialization of new technologies. The document describes two case studies of olefin hydrogenation using Vulcan catalysts. Both cases require a recycle stream to control exotherms. The results show the reactor sizing and operating parameters needed to meet a 5-year minimum catalyst life for both cases.
Study 1: Concept Hazard Review
CONTENTS
1.0 PURPOSE
1.0.1 Team
1.0.2 Timing
1.0.3 Preparation
1.0.4 Documentation
HAZARD STUDY 1: APPLICATION
1.1 Project Definition
1.2 Process Description
1.3 Materials Hazards
1.4 External Authorities
1.5 Organization and Human Factors
1.6 Additional Activities to be Completed
1.7 Review of Hazard Study 1
APPENDICES
A Chemical Hazard Guide Diagram
B Safety Risk Criteria - Limit Values for Tolerable Risk
C List of Additional Assessments
Application of Process to Management of Change and ModificationsGerard B. Hawkins
Application of Process to Management of Change and Modifications
Hazard Study Process: GBHE-PGP-006
CONTENTS
1.0 PURPOSE
1.1 THE NEED FOR MODIFICATIONS
1.2 GENERAL DESCRIPTION OF A MODIFICATION
1.3 PRINCIPLES TO BE FOLLOWED
1.4 REPLACEMENT OF ’LIKE WITH LIKE’
1.5 REMOTE / SMALLER SITES
1.6 GENERAL GUIDANCE TO INDIVIDUALS DOING SHE ASSESSMENTS FOR MODIFICATIONS
1.7 MODIFICATIONS HAZARD STUDY DECISION MECHANISM
1.7.1 Purpose
1.7.2 Methodology
FIGURE 1 MODIFICATION FLOWCHART
M1 Title, description, registration and process flowsheet
Gate 1 Preliminary authorization
Table 1 Difference between a Modification and a Project
M2 Risk Assessment
Gate 2 Approval
M3 Detailed design and implementation
Gate 3 Pre-Commissioning check
M4 Commissioning
Gate 4 Commissioned
M5 Final review and file
APPENDIX
APPENDIX A CHECKLIST FOR MODIFICATIONS
APPENDIX B DOCUMENTATION PROMPT LIST
APPENDIX C TYPICAL MODIFICATION FORM
G1 PRELIMINARY AUTHORIZATION
M2 PRELIMINARY SSHE ASSESSMENT
G2 REVIEW PRELIMINARY SSHE ASSESSMENT
M3 DESIGN and ESTIMATION
SSHE ASSESSMENT
G3 APPROVAL
M4 DETAILED DESIGN AND IMPLEMENTATION
G4 PRE-COMMISSIONING CHECK
M5 COMMISSIONING
G5 COMMISSIONED
M6 FINAL REVIEW AND FILE
Integration of Rotary Positive Displacement Pumps into a ProcessGerard B. Hawkins
Integration of Rotary Positive Displacement Pumps into a Process
This Engineering Design Guide deals with:
(a) The specification of the pump duty for enquiries to be sent to pump vendors,
(b) The estimation of the characteristics and requirements of the pumps in order to provide preliminary information for design work by others.
It applies to pumps in Group 2 and 3 as defined in GBHE-EDS-MAC-21 Series, and is also an essential preliminary step for a pump in Group 1 whose final duty is negotiated with the chosen pump supplier.
It may be used for general-purpose pumps in Group 4; their duties when used in a support role are often inadequately defined, whereupon such pumps can be specified by reference to the manufacturer's data for a pump satisfactorily fulfilling the same process need.
STEAMING PROCEDURE FOR VULCAN STEAM REFORMING CATALYSTSGerard B. Hawkins
The document discusses procedures for steaming Vulcan steam reforming catalysts to recover from sulfur poisoning and carbon formation incidents. It describes maintaining steam flow at 30-40% of design levels and an outlet temperature above 780°C. Gas samples should be taken hourly to monitor CO2, CH4, H2S and SO2. Steaming is complete when CO2 levels stabilize over 2-3 samples after increasing the temperature. The process typically takes 12-24 hours to complete and closely monitors pressure drop and tube conditions. After steaming, the catalyst requires reduction before restarting hydrocarbon feed.
Hydrogen Plant Flowsheet - Effects of Low Steam RatioGerard B. Hawkins
Effect of Low Steam Ratio on the Steam Reformer
Effect of Low Steam Ratio on H T Shift & PSA
Effect of Low Steam Ratio on Gross Efficiency
Effect of Low Steam Ratio on Net Efficiency
Alternative schemes for improving heat recovery
Determination of Inert Gas in Anhydrous Ammonia
ANHYDROUS AMMONIA: DETERMINATION OF INERT GASES
SCOPE AND FIELD OF APPLICATION
This packed-column GC method is suitable for the determination of hydrogen, nitrogen, oxygen, argon and carbon monoxide in anhydrous ammonia. The determinations of the gases are linear in the range O-100 ppm v/v.
Introduction High temperature shift Catalysts
Low temperature shift catalysts
Catalyst storage, handling, charging and discharging
Health and safety precautions
Reduction and start-up of high temperature shift catalysts
Operation of high temperature shift catalysts
Reduction and start-up of low temperature shift catalysts
Operation of low temperature shift catalysts
Cast White Metal Bearings
1 SCOPE
2 BACKING MATERIAL
3 SURFACE
4 THICKNESS
5 CLEANING PROCEDURE
6 TINNING
7 WHITE METAL
8 BOND SOUNDNESS
9 WITNESSED INSPECTION
10 MACHINING
11 FINAL INSPECTION OF BOND FOR SEAL RINGS
APPENDIX
A - METHOD OF CALCULATING REFLECTANCE RATIO
Ammonia Synthesis Catalyst Chemistry and Operator TrainingGerard B. Hawkins
The document discusses ammonia synthesis catalysts including their formulation, production, and operation. Key points include:
1) Ammonia synthesis catalysts are typically based on magnetite that is reduced to form a porous iron structure. Promoters like alumina and potash boost activity and stability.
2) Catalyst production involves melting components to control precursor phases before milling to size.
3) The reaction favors high pressure and low temperature. Typical conditions are 350-530°C and 100-600 bar. Temperature and pressure balance kinetics and equilibrium.
H - Acid Caustic Fusion Stage
CONTENTS
0 INTRODUCTION
1 DESIGN INFORMATION
1.1 Reactor Type
1.2 Temperature Range
1.3 Pressure Range
1.4 Chemical System
2 BACKGROUND
3 KINETICS AND MECHANISM
4 MAXIMUM YIELD AND IMPLICATIONS FOR REACTOR DESIGN
5 USE OF DESIGN MODEL FOR START-UP AND MANUFACTURING MONITORING
6 BIBLIOGRAPHY
FIGURES
1 FUSION MODEL OUTLINE MECHANISM AND KINETIC SCHEME
2 TEST RUN OPTIMIZATION OF HEATING TIME 3600 kg/h STEAM
METHANOL PLANT - SHALE GAS FEED PRETREATMENT
CASE STUDY #091406
Case Background
A Methanol plant operator would like to examine the technical feasibility of using Shale Gas as a feedstock to their Methanol plant.
The first step in the Methanol production process is gas pretreatment. The purpose of gas pretreatment is to make the gas suitable for the downstream processes. There are two groups of compounds that are usually present in natural gas and that should be removed during pretreatment—the associate NGL and the sulfur-containing compounds. Some natural gas reservoirs may also have other trace components that must be removed, but these are not discussed here.
This case study examines the impact of CO2 (Carbon Dioxide) on the pre-treatment section design, performance and efficiency of ACME Methanol Plant’ feed gas pre-treatment section.
Case 1: Normal Shale Gas
Case 2: “Bad Gas”
Case 3: Low CO2
Case 4: High CO2
Avoiding Stress Corrosion Cracking of Carbon Low Alloy and Austenitic Stainl...Gerard B. Hawkins
Avoiding Stress Corrosion Cracking of Carbon Low Alloy and Austenitic Stainless Steels in Chloride and Caustic Environments
SYNOPSIS
This Maintenance Best Practice Guide is concerned with the performance of carbon and low alloy steels, and austenitic stainless steels, in chloride and caustic containing fluids. Those factors which are known to promote stress corrosion cracking are outlined, and service charts defining environmental boundaries for stress corrosion cracking in caustic and chloride containing fluids are presented.
General guidance on the avoidance of stress corrosion cracking is provided.
Shortcut Methods of Distillation Design
0 INTRODUCTION/PURPOSE
1 SCOPE
2 ESTIMATIONOF PLATEAGE AND REFLUX
REQUIREMENTS
2.1 Generalized Procedure for Nmin and Rmin
2.2 Equation based Procedure for Nmin and Rmin
3 PREDICTION OF OVERALL PLATE EFFICIENCY
4 SIZING OF MAIN PLANT ITEMS
4.1 Column Diameter
4.2 Surface Area of Condensers and Reboilers
FIGURES
1 NON-IDEAL EQUILIBRIUM CURVE
2 AT A GLANCE CHART BASED ON FENSKE,
UNDERWOOD
3 PLATE EFFICIENCY CORRELATION OF O’CONNEL
VLE Data - Selection and Use
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 DIAGRAMMATIC REPRESENTATION OF IDEAL
AND NON-IDEAL SYSTEMS
4.1 Ideal Mixtures
4.2 Non-Ideal Mixtures
5 REVIEW OF VLE MODELS
5.1 Ideal Behavior in Both Phases
5.2 Liquid Phase Non-Idealities
5.3 High Pressure Systems
5.4 Special Models
6 SETTING UP A VLE MODEL
6.1 Define Problem
6.2 Select Data
6.3 Select Correlation(s)
6.4 Produce Model
7 AVOIDING PITFALLS
7.1 Experimental Data is Better than Estimates
7.2 Check Validity of Fitted Model
7.3 Check Limitations of Estimation Methods
7.4 Know Your System
7.5 Appreciate Errors and Effects
7.6 If in Doubt – Ask
8 A CASE STUDY
8.1 The Problem
8.2 The System
8.3 Data Available
8.4 Selected Correlation
8.5 Simulation
8.6 Selection of Model
9 RECOMMENDED READING
10 VLE EXPERTS IN GBHE
APPENDICES
A USE OF EXTENDED ANTOINE EQUATION
B USE OF WILSON EQUATION
C USEFUL METHODS OF ESTIMATING
D EQUATIONS OF STATE FOR VLE CALCULATIONS
TABLES
1 SUMMARY OF VLE METHODS
2 LIST OF USEFUL REFERENCES
FIGURES
1 VAPOR-LIQUID EQUILIBRIUM - IDEAL SOLUTION
BEHAVIOR
2 VAPOR-LIQUID EQUILIBRIUM - A GENERALISED
Y-X DIAGRAM
3 VAPOR-LIQUID EQUILIBRIUM - MINIMUM BOILING
AZEOTROPE
4 VAPOR-LIQUID EQUILIBRIUM - MAXIMUM BOILING
AZEOTROPE
5 VAPOR-LIQUID EQUILIBRIUM - MINIMUM BOILING
AZEOTROPE -TWO LIQUID PHASES
6 SENSITIVITY TO ERROR IN VLE DATA (BASED ON FENSKE EQUATION)
7(a) FITTING WILSON 'A' VALUES TO VLE DATA - CASE A
7(b) FITTING WILSON 'A' VALUES TO VLE DATA - CASE B
7(c) FITTING WILSON 'A' VALUES TO VLE DATA - CASE C
Distillation Sequences, Complex Columns and Heat IntegrationGerard B. Hawkins
Distillation Sequences, Complex Columns and Heat Integration
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 SEQUENCING OF SIMPLE COLUMNS
4.1 Sidestream Columns
4.2 Multi-Feed Columns
5 SIMPLE COLUMN SEQUENCING AND HEAT
INTEGRATION INTERACTIONS
5.1 Energy Quantity and Quality
5.2 Heat Integration within the Total Flowsheet
6 COMPLEX COLUMN ARRANGEMENTS
6.1 Indirect Sequence with Vapor Link
6.2 Sidestream Systems
6.3 Pre-Fractionator Systems
7 COMPLEX COLUMNS AND HEAT INTEGRATION
INTERACTIONS
FIGURES
1 DIRECT AND INDIRECT SEQUENCES
2 A SINGLE SIDESTREAM COLUMN REPLACING 2
SIMPLE COLUMNS
3 A TYPICAL MULTI-FEED COLUMN
4 TYPICAL GRAND COMPOSITION CURVE
5 TYPICAL INDIRECT SEQUENCE WITH VAPOUR LINK
6 SIDESTREAM STRIPPER AND SIDESTREAM
RECTIFIER
7 SIMPLEST PRE-FRACTIONATOR SYSTEM
8 SIMPLEST PRE-FRACTIONATOR SYSTEM
9 PETLYUK COLUMN
Adiabatic Reactor Analysis for Methanol Synthesis Plant Note Book Series: P...Gerard B. Hawkins
The document discusses adiabatic reactor analysis for methanol synthesis from syngas. It provides the reaction kinetics and calculates conversion, temperature, and reactor volume needed at different conversions. Energy and mass balances are used to derive relationships between conversion, temperature and reaction rate. Data is generated to plot conversion versus volumetric flow rate for reactor sizing. The plot indicates a continuous stirred tank reactor (CSTR) could achieve 85% conversion before switching to a plug flow reactor (PFR) for higher conversion with less volume.
This document provides an engineering design guide for pumps used in ammonium nitrate service. It discusses the properties of ammonium nitrate and its solutions, including decomposition, combustion, detonation, density, viscosity, vapor pressure, and freezing point. It also covers the calculation of pump duty, choice of pump type (centrifugal, rotary, reciprocating), recommended line diagrams, construction features of different pump types, materials of construction, and appendices on bearing lubricants. The guide is intended to help with the integration and design of pump systems for handling ammonium nitrate and its solutions in industrial processes.
Typical Stabilizer Chloride Management Problems
What Causes NH4Cl Salts?
Mitigating System Fouling
Operating practices
Problems with Water Injection
Design To Mitigate Salt Formation
Prevention
Remove Nitrogen from the feed
Remove chloride from stabilizer feed
Chloride Guard Bed
Caustic Injection
Water Wash
Summary
This document provides guidance on residence time distribution (RTD) data for process engineers. It discusses:
1) How RTD data measures mixing in reactors and can be used to model reactor performance.
2) Examples of how RTD data can model reactors for first and second order reactions, and the differences between micro and macromixing models.
3) Techniques for measuring RTD using radioactive tracers and modeling results based on the measured curves.
CONTENTS
1 SCOPE
2 PROPERTIES OF FLUID
2.1 General Properties of Sodium Hydroxide
2.2 Physical Properties of Sodium Hydroxide and its Solutions
2.3 Chemical Properties and uses of Sodium Hydroxide
2.4 Physiological effects of Sodium Hydroxide
2.5 Specifications of Commercial Caustic Soda Grades
3 CHOICE OF PUMP TYPE
3.1 Pump Duty
3.2 Pump Type
4 RECOMMENDED LINE DIAGRAMS
5 RECOMMENDED LAYOUT
6 CONSTRUCTION FEATURES
7 MATERIALS OF CONSTRUCTION
7.1 Nickel and Nickel Alloys
7.2 Austenitic Stainless Steel
7.3 Aluminium, Aluminium Alloys, etc.
7.4 Non-Metallic Materials
TABLES
1 PHYSICAL PROPERTIES (Solid Form)
2 PHYSICAL PROPERTIES (Solution Form)
3 CAUSTIC SODA GRADES
FIGURES
1.1 LINE DIAGRAM - HORIZONTAL GLANDED, GLANDLESS AND VERTICAL IN-LINE PUMPS
1.2 LINE DIAGRAM - VERTICAL SPINDLE CANTILEVER PUMPS
1.3 LINE DIAGRAM - SELF PRIMING PUMPS
1.4 LINE DIAGRAM - RECIPROCATING PLUNGER METERING PUMPS
1.5 LINE DIAGRAM - POSITIVE DISPLACEMENT DIAPHRAGM METERING PUMPS
1.6 WATER FLUSHING ARRANGEMENT FOR DOUBLE MECHANICAL SEAL
1.7 WATER FLUSH (QUENCH) ARRANGEMENT FOR SINGLE HARD FACED (CARBIDE) SEAL AND BACK-UP LIP SEAL
2 PHASE DIAGRAM OF NaOH-H2O
3 VISCOSITY OF AQUEOUS CAUSTIC SODA SOLUTIONS
4 VAPOR PRESSURE OF AQUEOUS CAUSTIC SODA SOLUTIONS
5 ENTHALPY CONCENTRATION FOR AQUEOUS CAUSTIC SODA SOLUTIONS
6 SPECIFIC GRAVITY FOR AQUEOUS CAUSTIC SODA SOLUTIONS
7 DILUTION OF CAUSTIC SODA LIQUOR
8 THERMAL CONDUCTIVITY OF AQUEOUS CAUSTIC SODA SOLUTIONS
9 SPECIFIC HEAT OF CAUSTIC SODA SOLUTIONS
10 BOILING POINTS OF STRONG CAUSTIC SODA SOLUTIONS AT REDUCED PRESSURE
11 COMMENCEMENT OF FREEZING OF CAUSTIC SODA SOLUTIONS (0 - 52% W/W)
12 TEMPERATURES ATTAINED ON DISSOLUTION OF ANHYDROUS CAUSTIC SODA
13 HEAT OF SOLUTION FOR ANHYDROUS CAUSTIC SODA
14 SOLUBILITY OF SODIUM CHLORIDE IN CAUSTIC SODA SOLUTIONS
15 DENSITY - CONCENTRATION TABLES FOR CAUSTIC SODA SOLUTIONS AT 600 F (15.5 0 C)
16 MATERIAL SELECTION CHART FOR CAUSTIC SODA HANDLING
Mixing of Immiscible Liquids
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 EQUIPMENT
4.1 Agitated Tanks
4.2 Flow Mixers
4.3 'High Shear' Mixers
5 SYSTEM PHYSICAL PROPERTIES
5.1 Density
5.2 Viscosity
5.3 Interfacial Tension
6 STIRRED VESSELS
6.1 Design for Complete Dispersion
6.2 Prediction of Phase Inversion
6.3 Design for Mass Transfer
6.4 Design for Dispersed Phase Mixing
6.5 Hold-Up in Continuous Vessels
7 FLOW MIXERS
7.1 Design for Turbulent Conditions
7.2 Design for Laminar Conditions
TABLES
1 REYNOLDS NUMBER RANGES
FIGURES
1 STANDARD TANK CONFIGURATION
2 EXPERIMENTAL RELATIONSHIP BETWEEN MASS
TRANSFER COEFFICIENT AND POWER DENSITY
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).
This document provides guidelines for engineering design of pressure relief systems. It discusses key principles such as identifying potential overpressure and underpressure causes, sizing relief systems to prevent hazards, and safely disposing of relieved materials. The guidelines cover statutory requirements, recommended design procedures, and documentation standards. The overall goal is to preserve equipment integrity and prevent failure from over or under pressure during all process phases.
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
101 Things That Can Go Wrong on a Primary Reformer - Best Practices GuideGerard B. Hawkins
This document discusses common problems that can occur in primary reformers and associated equipment. It identifies issues that can lead to plant shutdowns or efficiency losses, grouping them under catalysts, tubes, furnace boxes, burners, flue gas ducts, headers, and refractories. Some examples discussed include carbon formation, tube overheating, flame impingement, leaks in air preheaters, combustion air maldistribution, and damage to coffins. The document provides an overview of these issues to improve plant reliability over its lifespan.
El impacto en el rendimiento del catalizador por envenenamiento y ensuciamien...Gerard B. Hawkins
El documento describe los procesos de refinería y catalizadores, así como los efectos del envenenamiento y ensuciamiento en el rendimiento de los catalizadores. El envenenamiento reduce la actividad de los catalizadores al bloquear los sitios activos o modificar la química de la superficie, lo que afecta la actividad y selectividad. Los niveles bajos de contaminantes tienen un mayor impacto en catalizadores con menor área de superficie. El envenenamiento también puede causar cambios estructurales en el catalizador y permitir
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
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
Amine Gas Treating Unit - Best Practices - Troubleshooting Guide Gerard B. Hawkins
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
El documento proporciona una descripción general de los servicios y tecnologías de procesamiento de catalizadores de GBH Enterprises Ltd. (GBHE), incluyendo refinación de petróleo, procesamiento de gas, industrias petroquímicas y venta de catalizadores. GBHE ofrece servicios de ingeniería, soporte técnico y consultoría, así como una línea de catalizadores patentados para aplicaciones como desulfuración y purificación de gas.
Burner Design, Operation and Maintenance on Ammonia PlantsGerard B. Hawkins
The document discusses burner design, operation, and maintenance on ammonia plants. It covers reformer burner types and designs, including premix and staged burners. It also addresses combustion characteristics like excess air and fuel viscosity effects. Maintenance best practices like checking burner pressures and atomizing steam temperatures are emphasized. Low NOx equipment uses techniques like staged air, fuel, and flue gas recirculation to reduce emissions. Good combustion requires attention to design, operation, maintenance, and partnership among related roles.
Maruthi Prithivirajan, Head of ASEAN & IN Solution Architecture, Neo4j
Get an inside look at the latest Neo4j innovations that enable relationship-driven intelligence at scale. Learn more about the newest cloud integrations and product enhancements that make Neo4j an essential choice for developers building apps with interconnected data and generative AI.
UiPath Test Automation using UiPath Test Suite series, part 5DianaGray10
Welcome to UiPath Test Automation using UiPath Test Suite series part 5. In this session, we will cover CI/CD with devops.
Topics covered:
CI/CD with in UiPath
End-to-end overview of CI/CD pipeline with Azure devops
Speaker:
Lyndsey Byblow, Test Suite Sales Engineer @ UiPath, Inc.
Dr. Sean Tan, Head of Data Science, Changi Airport Group
Discover how Changi Airport Group (CAG) leverages graph technologies and generative AI to revolutionize their search capabilities. This session delves into the unique search needs of CAG’s diverse passengers and customers, showcasing how graph data structures enhance the accuracy and relevance of AI-generated search results, mitigating the risk of “hallucinations” and improving the overall customer journey.
Goodbye Windows 11: Make Way for Nitrux Linux 3.5.0!SOFTTECHHUB
As the digital landscape continually evolves, operating systems play a critical role in shaping user experiences and productivity. The launch of Nitrux Linux 3.5.0 marks a significant milestone, offering a robust alternative to traditional systems such as Windows 11. This article delves into the essence of Nitrux Linux 3.5.0, exploring its unique features, advantages, and how it stands as a compelling choice for both casual users and tech enthusiasts.
Infrastructure Challenges in Scaling RAG with Custom AI modelsZilliz
Building Retrieval-Augmented Generation (RAG) systems with open-source and custom AI models is a complex task. This talk explores the challenges in productionizing RAG systems, including retrieval performance, response synthesis, and evaluation. We’ll discuss how to leverage open-source models like text embeddings, language models, and custom fine-tuned models to enhance RAG performance. Additionally, we’ll cover how BentoML can help orchestrate and scale these AI components efficiently, ensuring seamless deployment and management of RAG systems in the cloud.
Pushing the limits of ePRTC: 100ns holdover for 100 daysAdtran
At WSTS 2024, Alon Stern explored the topic of parametric holdover and explained how recent research findings can be implemented in real-world PNT networks to achieve 100 nanoseconds of accuracy for up to 100 days.
Observability Concepts EVERY Developer Should Know -- DeveloperWeek Europe.pdfPaige Cruz
Monitoring and observability aren’t traditionally found in software curriculums and many of us cobble this knowledge together from whatever vendor or ecosystem we were first introduced to and whatever is a part of your current company’s observability stack.
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.
I, a former op, would like to extend an invitation to all application developers to join the observability party will share these foundational concepts to build on:
For the full video of this presentation, please visit: https://www.edge-ai-vision.com/2024/06/building-and-scaling-ai-applications-with-the-nx-ai-manager-a-presentation-from-network-optix/
Robin van Emden, Senior Director of Data Science at Network Optix, presents the “Building and Scaling AI Applications with the Nx AI Manager,” tutorial at the May 2024 Embedded Vision Summit.
In this presentation, van Emden covers the basics of scaling edge AI solutions using the Nx tool kit. He emphasizes the process of developing AI models and deploying them globally. He also showcases the conversion of AI models and the creation of effective edge AI pipelines, with a focus on pre-processing, model conversion, selecting the appropriate inference engine for the target hardware and post-processing.
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1. GBH Enterprises, Ltd.
Plant Analytical Techniques
BENFIELD LIQUOR: DETERMINATION OF IRON
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2. Benfield Liquor: Determination of Iron
1
SCOPE AND FIELD OF APPLICATION
This method is suitable for the determination of the total iron in Benfield
liquor samples up to a concentration of approximately 100 ppm m/v.
2
PRINCIPLE
A solution containing a compound of the metallic element under
investigation is aspirated into the flame of an atomic absorption
spectrophotometer, causing evaporation of the solvent and leaving a solid
residue. This process is rapidly followed by vaporization of the solid
residue with concomitant molecular dissociation into its constituent atoms
which are capable of absorbing radiant energy. The absorption of the
radiation from the light source by the atomic vapor is measured and
displayed by the spectrophotometer, in graphical format.
3
REAGENTS
During the analysis, use only reagents of analytical reagent grade, unless
otherwise specified, and water which has been deionized and then
distilled from an all glass apparatus, or water of equivalent purity.
3.1
Hydrochloric acid (SG 1.18)
THIS REAGENT CAUSES BURNS AND PRODUCES A HARMFUL VAPOR.
3.2
Ferric nitrate, standard spectroscopic solution in approximately 0.5
mol/L nitric acid. 1 mL = 1.00 mg iron
3.3
Stock standard iron solution: dilute 10 mL of the ferric nitrate
solution (3.2) to 100 mL with water in a one-mark volumetric flask. 1
mL = 100 µg Iron
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3. 3.4
4
Working standard iron solutions: dilute 2.5 and 5.0 mL of the stock
standard iron solution (3.3) to 100 mL with water in four one-mark
volumetric flasks. These working standard solutions will be
equivalent to 2.5 and 5.0 µg/m.l (ie ppm m/v) iron respectively.
APPARATUS
4.1
Standard volumetric glassware, class A.
4.2
Atomic absorption spectrophotometer. A Philips PU 9400 model,
or similar, is suitable.
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4. 5
PROCEDURE
5.1
Test portion, and preparation of the test solution.
Pipette 5.0 ml of test sample into a glass beaker then add 15 ml of
hydrochloric acid (3.1). Heat to dissolve any precipitate, if evident,
then allow to cool and transfer to a 100 ml one-mark volumetric
flask Dilute to the mark with water.
5.2
Blank solution
Prepare a blank solution, using the same reagent quantities as for
the test solution (5.1), but omitting the test portion.
5.3
Determination
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5. 5.3.1 The operating conditions for the atomic absorption
spectrophotometer (4.2) are as follows:
Lamp - iron hollow cathode;
Wavelength - 248.3 nm;
Band pass - 0.2-0.5 nm;
Flame - air/acetylene, fuel lean, blue.
5. 3.2 Aspirate, the lowest concentration working standard solution
(3.4), the blank solution (5.2), the rest of the working standard
solutions, and the test solution (5.1). consecutively into the atomic
absorption spectrophotometer (4.2). in accordance with the
manufacturer's instructions.
ASPIRATE THE WORKING STANDARD SOLUTIONS CONSECUTIVELY
FROM THE LOWEST TO THE HIGHEST CONCENTRATION.
TEST SAMPLES OF IRON CONCENTRATION > 50 PPM M/V MUST BE
FURTHER DILUTED TEN-FOLD PRIOR TO ASPIRATION.
5. 3.3 The atomic absorption spectrophotometer will establish the
absorbance-concentration relationship to give the concentration equivalent
of the measured test solution absorbance.
6
EXPRESSION OF RESULTS
6.1 The iron in the test solution (5.l), expressed as ppm m/v, is given by
automated interpolation from the standard curve displayed on the atomic
absorption spectrophotometer.
6.2 As dilution of the test portion is necessary, the iron in the test
sample, expressed as ppm m/v, is given by the expression
C1 x V2
V1
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6. Where
C1 is the concentration of iron in the test solution (in ppm m/v) derived
automatically from the standard curve;
V2 is the volume of the test solution n (in mL, ie 100 mL);
V1 is the volume of the test portion taken for dilution (in mL; ie 5.0 mL.);
6.3 For test samples of iron concentration > 50 ppm m/v, a further tenfold dilution of the test solution will be necessary. The iron, expressed as
ppm m/v, is given by the expression
C1 x V2 x 10
V1
Refinery Process Stream Purification Refinery Process Catalysts Troubleshooting Refinery Process Catalyst Start-Up / Shutdown
Activation Reduction In-situ Ex-situ Sulfiding Specializing in Refinery Process Catalyst Performance Evaluation Heat & Mass
Balance Analysis Catalyst Remaining Life Determination Catalyst Deactivation Assessment Catalyst Performance
Characterization Refining & Gas Processing & Petrochemical Industries Catalysts / Process Technology - Hydrogen Catalysts /
Process Technology – Ammonia Catalyst Process Technology - Methanol Catalysts / process Technology – Petrochemicals
Specializing in the Development & Commercialization of New Technology in the Refining & Petrochemical Industries
Web Site: www.GBHEnterprises.com
7. Refinery Process Stream Purification Refinery Process Catalysts Troubleshooting Refinery Process Catalyst Start-Up / Shutdown
Activation Reduction In-situ Ex-situ Sulfiding Specializing in Refinery Process Catalyst Performance Evaluation Heat & Mass
Balance Analysis Catalyst Remaining Life Determination Catalyst Deactivation Assessment Catalyst Performance
Characterization Refining & Gas Processing & Petrochemical Industries Catalysts / Process Technology - Hydrogen Catalysts /
Process Technology – Ammonia Catalyst Process Technology - Methanol Catalysts / process Technology – Petrochemicals
Specializing in the Development & Commercialization of New Technology in the Refining & Petrochemical Industries
Web Site: www.GBHEnterprises.com