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Introduction to Process Safety Engineering Lessons learned from incidents By Geert Vercruysse PS Conference, Dordrecht, 30 th May 2018

Introduction to Process Safety Engineering Lessons learned from …pscongres.nl/wp-content/uploads/2016/06/12-BASF-Geert-Vercruysse... · Distillation Columns Flare PSH Atmosphere

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Page 1: Introduction to Process Safety Engineering Lessons learned from …pscongres.nl/wp-content/uploads/2016/06/12-BASF-Geert-Vercruysse... · Distillation Columns Flare PSH Atmosphere

Introduction to Process Safety Engineering

Lessons learned from incidents

By Geert Vercruysse

PS Conference, Dordrecht, 30th May 2018

Page 2: Introduction to Process Safety Engineering Lessons learned from …pscongres.nl/wp-content/uploads/2016/06/12-BASF-Geert-Vercruysse... · Distillation Columns Flare PSH Atmosphere

8 Safety Functions for a Chemical Plant

1. Prevention of loss of containment due to process upsets

2. Prevention of loss of containment due to degradation.

3. Limitation of the size of an accidental release.

4. Control of spreading of substance accidentally released.

5. Prevention of ignition of explosive atmospheres.

6. Mitigation of damage due to fire.

7. Mitigation of damage due to explosion.

8. Mitigation of damage due to toxic release.

Cfr. Presentation by FOD WASO

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Layers of Protection

M

I

T

I

G

A

T

I

O

N

P

R

E

V

E

N

T

I

O

N

Geert Vercruysse Process Safety Congress, Dordrecht, 30 May 2018 3

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Introduction

Batch Reactor Distillation Column

• Widely used

• Small volume applications

• General-purpose equipment can be

shared between several products &

processes

• By nature of batch operation no

steady state operation

• Secure follow up of the sequence of

the process steps – mimick “golden

batch” typical

• Objective: separation of mixtures in

pure components or different

fractions.

• Technology is energy intensive as

separation is based on gas / liquid

interchange.

• “Internals” in a distillation column will

not be further discussed. No

fundamental difference in equipment

design conditions nor process safety

concept.

Geert Vercruysse Process Safety Congress, Dordrecht, 30 May 2018 4

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Introduction

As technologies in the process industry are energy intensive there is a

strong focus on the overpressure protection.

This means that when a failure occurs the design conditions

(pressure/temperature) should not be exceeded.

Additionally it’s important to know and understand the background and

dimensioning of the safety concept, especially for the evaluation of

MOC’s (Management of Change – on all changes).

In the next slide some generic failures are presented which should be

included in the Process Hazard Analysis (PHA).

Geert Vercruysse Process Safety Congress, Dordrecht, 30 May 2018 5

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Batch Polymerisation Reactor –

Process Safety Scenarios

Geert Vercruysse Process Safety Congress, Dordrecht, 30 May 2018 6

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Distillation –

Process Safety Scenarios

Geert Vercruysse Process Safety Congress, Dordrecht, 30 May 2018 7

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Overpressure Protection

Distillation Columns

Flare

PSH

Atmosphere

OPEN

Design

Relief valve

CLOSE

Design

SIL-interlock

NA

Design

Intrinsic Safe

Flare

PSH

CLOSE

Design

SIL-interlock

Flare

Mechanical Safety Concept Instrumental Safety ConceptIntrinsic safe

Geert Vercruysse Process Safety Congress, Dordrecht, 30 May 2018 8

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Mechanical Safety Concept

Relief devices are ususally designed to protect the equipment and auxillaries from

overpressure due to any single cause.

The probability of two unrelated failures occurring simultaneously is considered

remote and is not normally designed for.

API RP 521 defines causes to be unrelated if no process, mechanical or electrical

linkages exist among them.

Geert Vercruysse Process Safety Congress, Dordrecht, 30 May 2018 9

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Instrumentational Safety Concept

Safety instrumented functions are ususally designed to protect the equipment and

auxillaries from overpressure due to different type of causes.

IEC 61511 is the guideline used in EMEA.

Specific engineering concepts:

Functional safety – the complete set up from sensor till actor is described.

“Voting systems” 1oo1, 1oo2, 2oo3, …

Complexity requires on line testing – calibration.

Geert Vercruysse Process Safety Congress, Dordrecht, 30 May 2018 10

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Process Safety … still more to be done

Process Safety … still more to be done :

Process Safety Incidents (LOPC) are investigated and root causes are

addressed.

Time Incident

Nov 2013 Steam clamp explosion at Total Antwerp

Jun 2014 Explosion at Shell Moerdijk

Jan 2015 Pipe rupture and Explosion at BASF Antwerp

Feb 2016 Runaway and explosion at Indaver Antwerp

Oct 2016 HP Ethylene pipe explosion at BASF Lu

Aug 2017 Furnace Fire at Exxon Refinery

Geert Vercruysse Process Safety Congress, Dordrecht, 30 May 2018 11

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Process Safety … still more to be done

Industry 4.0

Further focus on :

Prevention of loss of containment due to process upsets.

Prevention of loss of containment due to degradation.

Prevention of human and organizational errors.

Industry 4.0 will lead to better tools to tackle main root causes leading to Process

Safety Incidents :

Specific tool for isolation management.

Improved communication tools between operating teams and maintenance.

Visualization tool for permits and process systems – improve decision making for

emergency management.

Geert Vercruysse Process Safety Congress, Dordrecht, 30 May 2018 12

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Industry 4.0

Improve Standard Operating Procedures

Geert Vercruysse Process Safety Congress, Dordrecht, 30 May 2018 13

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Process Safety … still more to be done

Know How & Competence

Geert Vercruysse Process Safety Congress, Dordrecht, 30 May 2018 14

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Know How & Competence

Deliverables from the organization

Technology

groupPlant

Manager

Inspection

group

ESH-

group

Process

Manager

Production

Manager

Asset

Manager

Global

Organization

Plant

Organization

Site

Organization

Experience Exchange

with similar units

Overview incidents

Process Safety Concepts

PFD’s

Overview

calculations

MOC’s

Projects

P&ID’s

Process Manual

Written

procedures

Training

SAP History

Prev. Maint. Plan

Test freq.

& reports

Techn.

Document.

Inspection plan

Inspection

reports

Expertise

(e.g. corrosion)

ESH legal

guidelines

ESH corporate

guidelines

Expertise

(e.g. relevant

incidents)

Geert Vercruysse Process Safety Congress, Dordrecht, 30 May 2018 15

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Conclusions

Recent incidents shows further need to focus on know how and

competence.

During revalidation of process safety study important incidents need to be

incorporated in safety concept (“Lessons Learned”).

Many have to do with start up or non-routine activities – new tools are

under development to support Operations & Maintenance.

“Keep the memory alive”

Geert Vercruysse Process Safety Congress, Dordrecht, 30 May 2018 16

Page 17: Introduction to Process Safety Engineering Lessons learned from …pscongres.nl/wp-content/uploads/2016/06/12-BASF-Geert-Vercruysse... · Distillation Columns Flare PSH Atmosphere

We create chemistry

that makes questions love

answers.