Sulphur Melting An Overview 1 SANDVIK PROCESS SYSTEMS THE - - PowerPoint PPT Presentation

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Sulphur Melting An Overview 1 SANDVIK PROCESS SYSTEMS THE - - PowerPoint PPT Presentation

Sulphur Melting An Overview 1 SANDVIK PROCESS SYSTEMS THE INDUSTRIAL PROCESSING COMPANY Agenda Sulphur Melting Strategy Before You Melt Sulphur Melting Technologies Footprint Comparison Sulphur Contamination


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SLIDE 1

Sulphur Melting – An Overview

1

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SLIDE 2

SANDVIK PROCESS SYSTEMS

THE INDUSTRIAL PROCESSING COMPANY

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SLIDE 3

Agenda

3

Sulphur Melting Strategy

Before You Melt

Sulphur Melting Technologies

 Footprint Comparison 

Sulphur Contamination

 Sulphuric Acid 

Material Selection

Melt Rate

Sulphur Block Reclaim

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SLIDE 4

Sulphur Melting Strategy

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Why does sulphur need to be melted?

Consumer requires liquid sulphur as a feed stock

Examples: Sulphuric acid plant, fertilizer plant

Sulphur needs to be converted to a marketable form

Examples: Processing a sulphur block, cleanup of leak from liquid system or spillage from conveying system

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SLIDE 5

Before You Melt

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Desired capacity

Solid sulphur feed stock specifications

Liquid sulphur specifications

Operator considerations

Emissions considerations

Site and footprint considerations

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SLIDE 6

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Sulphur Melting Technologies

Melter Movement: Stationary vs. Mobile

Heat Transfer:

Immersion vs. Surface

Agitation vs. Stagnant

Internal vs. External

Feed System: Continuous vs. Batch

Emissions Management: Open-top vs. Contained

Contaminate Removal: Automatic vs. Manual

Construction: In-ground vs. Stick-built

  • vs. Skid-package
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SLIDE 7

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Continuous, Immersion, Agitation

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SLIDE 8

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  • Skid Area X 3 = Sulphur Pit Area
  • Pit Depth = 3 meters below ground
  • Skid Platform Height = 3 meters above ground

Stagnant Batch (Pit) vs. Agitation with Continuous Feed (Skid)

Immersion Melting – Footprint Comparison

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SLIDE 9

Sulphur Contamination

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Solid contaminates

Sand, Rocks

Carsul

Clay

Liquid contaminates

H2O

H2SO4 (sulphuric acid)

Hydrocarbons, Amines, Glycol

Gaseous contaminates

H2S, SO2

Sulphur Vapour (Dust)

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SLIDE 10

Sulphuric Acid

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How it happens (2S + 2H2O + 3O2 = 2H2SO4)

Impact / Neutralization

Prevention

 Keep the sulphur dry!  Sodium Lauryl Sulfate (SLS) 

Strategy

 SLS / Vancouver Port strategy

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SLIDE 11

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Material Selection

Corrosion Mechanisms

 Wet Sulphur Corrosion  Sulphuric Acid Corrosion 

Carbon Steel

Stainless Steel

Cost vs. Benefit

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SLIDE 12

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  • Available Surface Area
  • Particle Size
  • Ambient Temperature
  • Moisture

Factors to Consider:

Melt Rate

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SLIDE 13

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  • Smaller particles = more surface area = higher heat transfer capability
  • Mass: (1) 100 mm diameter particle = (4000) 6 mm diameter particles = 1.14 kg
  • Surface Area:

(1) 100 mm particle = 0.032 m2 (4000) 6 mm particles = 0.52 m2 (16X)

Immersion Melting Relationship

Melt Rate – Particle Size

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SLIDE 14

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200 400 600 800 1000 1200 1400 1600

  • 20
  • 15
  • 10
  • 5

5 10 15 20

Capacity (Metric Tonnes/Day) Ambient Temperature, °C

Production Capacity Vs. Ambient Temperature (Assuming 130 °C Sulphur Discharge T, 96% Availability)

0% H₂0 1% H₂0 2% H₂0 3% H₂0 4% H₂0 5% H₂0

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SLIDE 15

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Sulphur Block Reclaim

Melting needs to be considered in your block pouring strategy because it affects:

Size and configuration of block

Allowable contamination in block

Utility infrastructure

Dust control options

Availability of block

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SLIDE 16

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Sulphur Block Reclaim

Shah Example: Time required to melt 1.2 million tonnes (4 months production)

1000 TPD, 300 Days Per Year = 4 Years

2000 TPD, 300 Days Per Year = 2 Years

4000 TPD, 300 Days Per Year = 1 Year

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SLIDE 17

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Questions