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Mr. Julian Sowah – Qatalum Mr. Vivek Shroff – Qatalum

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Presentation on theme: "Mr. Julian Sowah – Qatalum Mr. Vivek Shroff – Qatalum"— Presentation transcript:

1 Startup and Tuning of Material Distribution System at Aluminium Smelter in Qatar
Mr. Julian Sowah – Qatalum Mr. Vivek Shroff – Qatalum Mr. Santosh Kumar – Qatalum Mr. Arne Hilck - Claudius Peters Mr. Jan Paepcke - Claudius Peters

2 Content of Today Introduction of Claudius Peters Aerated Distribution System for Potroom Feeding (ADS) – Basics Claudius Peters - Outlook for 2015 Introduction of Qatalum Startup and Tuning - Results Summary and Outlook 2015

3 ADS: Results of Qatalum Smelter
Outlook TMS 2013 for 2014 FLUIDCON: Attrition factor testing ADS: Results of Qatalum Smelter AS – System: Commissioning of Boguchany and Results

4 Introduction – Claudius Peters
Worldwide acting Engineering Company (born 1906) Main Business Areas: Aluminium, Cement, Steel, Gypsum, Power More than 550 employees worldwide Deliverer for AIRBUS Industries Turnover 150 Mio € Offices in Germany, USA, France, China, Brazil UK, Spain, Italy, Romania, Singapore, India

5 The ADS Principle

6 The ADS Principle

7 The ADS Principle

8 Introduction - Who are we?
Qatalum

9 Introduction Qatalum: Our Milestones
2004 2011 December Heads of agreement 2009 March Project completion ​September 21 Qatalum achieved full production of 585,000 tonnes 2007 2010 April Power from grid October First raw material ship November Commissioning of cast house December 18 First Metal from potline First Export of PFA January Site preparation start-up July Final approval November Construction commences January First EI Export Fuel gas for power plant gas turbines Initial power available from power plant 2006 March Joint venture agreement and approval of feasibility October Investment decision ​Qatalum is an equal joint venture between Qatar Petroleum and Hydro Aluminium of Norway and produces 585,000 tons of high-quality primary aluminium products per annum from twin 1.2 kilo​metre potlines Current production capacity exceeds 620,000 tonnes of aluminium

10 39 Nationalities at Qatalum
Qatalum: About Us 357 7 2 6 50 3 16 15 1 98 30 11 9 21 172 47 239 34 39 Nationalities at Qatalum 5

11 Reduction (Potlines) - Qatalum
Designed for low specific energy consumption, high labour productivity, low emissions, no SPL landfill 1.2 km x 704 pots 314 kA Delete text box and insert Picture/Photo/Figure here

12 Qatalum Delete text box and insert Picture/Photo/Figure here

13 Aerated Distribution System in operation since 2009

14 Qatalum Pot Line Design Parameters
Design Parameter (704 pots) Name Template Capacity Amperage Number of Pots Design 585,000 t/y 300 kA 704 Present Day + 605,000 t/y 314 kA Enter speaker notes here.

15 Qatalum ADS Design Parameters Distribution Air slide
ADS desgin parameters Distribution Air slide Inclination Cell Airslide Design 50 t/h 1 ° 10 [t/h] 0.5 ° Present Day 100 t/h 10 t/h Enter speaker notes here.

16 CHALLENGES Constant Flow into System with varying Material Properties
Silo fluidisation Silo aeration timing Material overflow from Silo to Coarse Particle Separator (CPS) Coarse Particle Separator (CPS) Accessibility & Performance Air supply nozzles (blockages) De-aeration of transport system Fine tuning of operational settings

17 Modifications carried out
Modification CPS for accessibility Repositioning of Level switches Conversion of level switches to adjustable types. Installation of additional manual valves on 750t secondary alumina silo Filling time optimization Provision of continous venting (2015)

18 Coarse Particle Separator
Improvements Baffle plates for flow control Vibrator design Silo fluidisation adjustment Aeration nozzle size repositioning Easier access for daily inspections

19 Coarse Particle Separator- Improvement Results
Month No. of CPS overflows Jul-12 26 Aug-12 32 Sep-12 34 Oct-12 28 Nov-12 29 Dec-12 30 Jan-13 11 Feb-13 5 Mar-13 2 Apr-13 May-13 4 Jun-13 Jul-13 Aug-13 Sep-13 Oct-13 13 Nov-13 3 Dec-13

20 Other Modifications Carried Out
Modification of CPS for accessibility Repositioning of Level switches on airslides Installation of adjustable level switches Additional manual valves on alumina silo 20

21 Verification of Improvements
How the improvements were measured Alumina spills on CPS Maintenance cost - No significant wear can be seen on the airslide fabric - Spare / Wear parts consumption is extremely low Timing of aeration system (Small increaments of 10s resulted in more consistent filling)

22 ADS – Results & Advantages
NO RISK for Potline – Easy catch up after stoppage. Easy maintenance. Low manpower. 2013 Maintenance cost = USD/ton of alumina Operational activities: Cleaning of CPS and visual inspections! System availibility is more than 98%; The buffer silosensures constant material supply to pots. Dust free system (environmentally friendly) No accumulation of coarse particles in the system, as material is screened out in the beginning. Little variations in alumina grain size distribution during conveying Always material supply for Potline – The System is able to catch up easily after several hours of stoppage of ADS-system,together with the buffer silos, this ensures constant material supply always. Easy maintenance. Low manpower. Activities: Only Cleaning of CPS and visual inspections! 2013 Maintenance cost = USD/ton of alumina Dust free system (environmentally friendly) No accumulation of coarse particles in the system, as material is screened out in the beginning. No significant variations in alumina grain size distribution during conveying

23 Variations in alumina grain size distribution during conveying
Longest Conveying distance = 280m Samples taken from various points starting from the silo outlet through to the farthest pot (280m away).

24 Particle Size Distribution/ Check
Ø 8,1% < 45µm Ø 8,21% < 45µm AH: New table, Added the averages of ADS PSD-evaluation, Result: At the beginning of the branch is nearly the same PSD compared to the end pots of each branch. Ø 8,3% < 45µm Ø 7,9% < 45µm

25 No Effect on PSD and Anode effect distribution
Material AH: new table, this shows the qualitative distribution of anode effects within a two-branch-system. If there would be a difference in particle size distribution, there would be an effect on anode effects as well. But this effect can not be seen, therefore the conclusion is: There is no negative effect from the distriution system on the PSD. Number of AE

26 ADS Maintenance No significant wear has been seen on the airslide fabric since the plant startup Spare / Wear parts consumption is extremely low

27 No Scaling No build-up of scales inside Airslides
No Coarse particle accumulation. AH: New slide showing the non existing scaling

28 Lessons Learned Material Flow from silo
Control of alumina flow out of silo / inlet box by optimization of aeration air. Coarse particle seperator upgrade Quality of aeration air/Aeration nozzles Flushing of the air system before start-up is helpful Selection of air filtration system for compressed air Stability of deaeration pressure is crucial for the system operation

29 Thank you for your attention


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