+ All Categories
Home > Documents > Refi neries. Oxygen for the Claus process.Linde-designed O 2 dosing system including a control...

Refi neries. Oxygen for the Claus process.Linde-designed O 2 dosing system including a control...

Date post: 14-Sep-2020
Category:
Upload: others
View: 1 times
Download: 0 times
Share this document with a friend
2
FLOWTRAIN ® is a registered trademark of The Linde Group. OXYMIX TM is a trademark of The Linde Group. Refineries. Oxygen for the Claus process. Reference customer Location Gas application Background Effects of O 2 enrichment Situation on site in 2005 Trials and measures Galp Energia Sines, Portugal O 2 enrichment for intensification of Claus processing Most oil refineries operate one or more Claus units for desulphurisation of gas streams rich in H 2 S and in many cases containing considerable amounts of ammonia (NH 3 ) as well. Mainly due to legal regulations regarding the reduction of sulphur content in fuels, the amount of H 2 S as well as NH 3 is increasing and often Claus units are becoming bottlenecks for the whole refinery. By enrichment of combustion air with O 2 , a Claus unit’s capacity in sulphur recovery can be increased significantly. A second beneficial effect is the fact that this raises the temperature within the Claus furnace, which in turn contributes to the stabilisation of the process, e.g. by more efficient destruction of NH 3 . The three Claus units operated in Sines covered a total capacity of 180 tons of sulphur per day. Mainly due to NH 3 in the Claus feed, long-term stability of Claus operation was limited. In addition, an increased amount of acid gas could be expected for the future and additional use of O 2 appeared to be the measure of choice to tackle both challenges simultaneously. In 2005, O 2 enrichment trials at two Claus units (including the determination of NH 3 destruction effectiveness) were performed in cooperation with Linde. The results clearly confirmed the expected effects; i.e. a consi- derable improvement of NH 3 destruction in the furnace and a sufficient capacity increase can be realised by this flexible, minor-investment solution. A long-term trial lasting more than a year was started in summer 2006. It led to a permanent implementation of O 2 enrichment. Galp Energia operates three Claus units at Portugal’s largest refinery in Sines (120 km south of Lisbon).
Transcript
Page 1: Refi neries. Oxygen for the Claus process.Linde-designed O 2 dosing system including a control system (FLOWTRAIN ®) and injector (OXYMIXTM) for application of gaseous oxygen Liquid

FLOWTRAIN® is a registered trademark of The Linde Group.OXYMIXTM is a trademark of The Linde Group.

Refi neries. Oxygen for the Claus process.

Reference customer

Location

Gas application

Background

Effects of O2 enrichment

Situation on site in 2005

Trials and measures

Galp Energia

Sines, Portugal

O2 enrichment for intensifi cation of Claus processing

Most oil refi neries operate one or more Claus units for desulphurisation of gas streams rich in H2S and in many cases containing considerable amounts of ammonia (NH3) as well. Mainly due to legal regulations regarding the reduction of sulphur content in fuels, the amount of H2S as well as NH3 is increasing and often Claus units are becoming bottlenecks for the whole refi nery.

By enrichment of combustion air with O2, a Claus unit’s capacity in sulphur recovery can be increased signifi cantly.A second benefi cial effect is the fact that this raises the temperature within the Claus furnace, which in turn contributes to the stabilisation of the process, e.g. by more effi cient destruction of NH3.

The three Claus units operated in Sines covered a total capacity of 180 tons of sulphur per day. Mainly due to NH3 in the Claus feed, long-term stability of Claus operation was limited. In addition, an increased amount of acid gas could be expected for the future and additional use of O2 appeared to be the measure of choice to tackle both challenges simultaneously.

In 2005, O2 enrichment trials at two Claus units (including the determination of NH3 destruction effectiveness)were performed in cooperation with Linde. The results clearly confi rmed the expected effects; i.e. a consi-derable improvement of NH3 destruction in the furnace and a suffi cient capacity increase can be realised by this fl exible, minor-investment solution.

A long-term trial lasting more than a year was started in summer 2006. It led to a permanent implementation of O2 enrichment.

Galp Energia operates three Claus units at Portugal’s largest refi nery in Sines (120 km south of Lisbon).

26448_Ref_DS_O2Claus2.indd 126448_Ref_DS_O2Claus2.indd 1 02.03.2009 14:28:01 Uhr02.03.2009 14:28:01 Uhr

Page 2: Refi neries. Oxygen for the Claus process.Linde-designed O 2 dosing system including a control system (FLOWTRAIN ®) and injector (OXYMIXTM) for application of gaseous oxygen Liquid

Tailored O2 injector OXYMIXTM implemented in the Claus unit’s process air pipe

Gaseous oxygen (GOX) supply train

Linde AGLinde Gases Division, Seitnerstrasse 70, 82049 Pullach, GermanyPhone +49.89.74 46-0, Fax +49.89.74 46-12 30, www.linde-gas.com

4348

8041

0

309

- 1.

1 L&

P S

ubje

ct t

o ch

ange

.

2 out of 3

50 tons of sulphur per day/plant

> 80 vol.-%

A few percent (due to SWS gas processing)

Selective H2S oxidation “Superclaus”

Optimised NH3 destruction and capacity increase (up to approx. 30 %)

28 vol.-%

3 Refi neries. Oxygen for the Claus process.

Number of Claus units operated with O2 enrichment

Capacities (air-only mode)

H2S in feed streams

NH3 in feed streams

Installed tailgas treatment

Main purpose of O2 application

Maximum O2 content in O2-enriched process air

O2 trials in cooperation with Linde

Start-up

Hardware

Mode of O2 supply

From 2005 to 2007

Routine operation with O2 enrichment since 2007

Linde-designed O2 dosing system including a control system (FLOWTRAIN®) and injector (OXYMIXTM) for application of gaseous oxygen

Liquid oxygen (LOX) via tank/vaporiser system

26448_Ref_DS_O2Claus2.indd 226448_Ref_DS_O2Claus2.indd 2 02.03.2009 14:29:01 Uhr02.03.2009 14:29:01 Uhr


Recommended