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High Temperature Solid Looping Cycles Network

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1st Meeting of the

High Temperature Solid Looping Cycles Network

Date: 15-17 September 2009

Oviedo, Spain

INCAR-CSIC Entrance

INCAR-CSIC Entrance

Organised by
IEA Greenhouse Gas R&D Programme

Co-Ordinators:
Carlos Abanades
Monica Alonso
and Mike Haines

Sponsored by

CSIC Logo Grupohunosa Logo
Endesa Logo

 

 

Lastest Information

Presentations made, now below in PDF format. Please see agenda for individial downloads.

Meeting Agenda PDF

 

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1. Background:

The international high temperature solid looping cycles network was adopted as an IEA GHG network in December 2008 and builds upon four preceding international workshops on in-situ CO2 removal organized largely by academia. The aim of the network is to promote further development and scale- up of processes for CO2 capture which involve solid looping cycles operating at elevated temperatures. At the industrial scale such processes are likely to use dual circulating fluid-bed technology, although fixed bed variants are also possible. The most notable applications are high temperature carbonation/ calcination (the forward and reverse steps of the reaction between CaO and CO2) to remove CO2 from flue gases or reformed gas streams as well as solid bed oxidation/reduction loops which allow a variant of oxy-combustion of fossil fuels. An aim of the network is to expand current participation beyond the research community to include potential operators, plant designers and equipment suppliers because the technology is starting to move from the bench scale to pilot and industrial demonstration scale.

1st Meeting:

The meeting should be a perfect opportunity to meet and discuss details at working level with those engaged like you in Research and Development activities on calcium looping cycles for post-combustion or for H2 production, oxygen chemical looping combustion and reforming, and other advanced CO2 capture systems involving reversible gas-solid reactions at high temperatures, that are moving fast towards scaling up and demonstration in large pilots.

The meeting will take place at the "Instituto Nacional del Carbón" INCAR-CSIC in Oviedo, Asturias, Spain (http://www.incar.csic.es).

 

 

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2. Provisional Agenda

Day 1 - Tuesday 15th September

12.00 - 13.00

Introductory Seminar: Sorption Enhanced Reforming; Prof. Douglas Harrison

15.00 - 15.30

Registration

15.30 - 16.00

Welcome and opening of the meeting; Vice President of CSIC (Spanish Research Council)

16.00 - 16.30

IEA GHG Activities and Networks; Mike Haines, IEA GHG

Technical Session 1 : Performance of Solid Materials (I)

16.30 - 16.50

C1: Ca looping technology developments; E J Anthony (CANMET-Canada) et al

16.50 - 17.10

C2: Novel calcium-based regenerative sorbents for high temperature CO2-capture; Julien Meyer (IFE-Norway)

17.10 - 17.30

C3: Development of long life-time CO2 sorbents based on CaO for high temperature applications; Angeliki Lemonidou (Aristotle University of Thessaloniki-Greece)

17.30 - 17.50

C4: Calcium based CO2 Capture Materials without the problem of loss-in-capacity; Bo Feng (University of Queensland-Australia)

17.50 - 18.20 Coffee Break

Technical Session 2 : Precombustion Ca-Looping (I)

18.20 - 18.40

C5: HyPr-RING process (In-Situ CO2 capture gasification) and its current results; Shiying Lin (Japan Coal Energy Center-Japan)

18.40 - 19.00

C6: Cyclic carbonations and calcinations of dolomite during sorption enhanced steam reforming of liquid bio-fuels; Valerie Dupont (University of Leeds-UK)

19.00 - 19.20

C7: A high temperature solids looping cycle for the conversion of a carbonaceous fuel in to H2 with simultaneous capture of the CO2; Christopher Bohn/John Dennis (University of Cambrige-UK)

19.20 - 19.40

C8: Flue-gas treatment by methane tri-reforming combined with lime carbonation and syngas production; Martin Halmann (Weizmann Institute of Science-Israel), and A Steinfeld, ETH Zurich

19.40 - 21.00 "Vino Español" (Wine Reception)

 

Day 2 - Wednesday 16th September

Technical Session 3 : Postcombustion Ca-Looping (I)

09.00 - 09.20

C9: The ENDEX configuration for CaO looping reactors; Marck Sceats (Calix-Australia)

09.20 - 09.40

C10: Ca-Looping processes with oxyfired CFBC regeneration; Angel Martínez (Foster Wheeler)

09.40 - 10.00

C11: Development of postcombustion CO2 capture with CaO in a large test facility: "CaOling"; Andrés Sánchez-Biezma (ENDESA-Spain)

10.00 - 10.20

C12: Activities within the German Research project "Limestone based absorption of CO2" (LISA); Bern Epple (Technical University of Darmstadt-Germany)

10.20 - 10.40

C13: Carbonation-Calcination Reaction Process for High Temperature Post Combustion CO2 and Sulfur Removal; L.S. Fan/ Shwetha Ramkuma (The Ohio State University-USA)

10.40 - 11.00 Coffee Break

Technical Session 4 : Postcombustion Ca-Looping (II)

11.00 - 11.20

C14: Design and Construction of a 200 kWth Calcium Looping Dual Fluidized Bed Facility for CO2 Capture; Heiko Dieter / Ajay Bidwe (Stuttgart University-Germany)

11.20 - 11.40

C15: Investigation of the Effect of Operational Parameters on CO2 Capture Efficiency on a 10 kWth Calcium Looping Dual Fluidized Bed Facility; Alexander Charitos (Stuttgart University-Germany)

11.40 - 12.00

C16: Continuous CO2 Capture from Flue Gas in Dual Fluidized Bed Reactors with Ca-based Sorbent; Li Zhenshan (Tsinghua University-China)

12.00 - 12.20

C17: Experimental investigation of a CFB reactor to capture CO2 from flue gases with CaO; Carlos Abanades (INCAR/CSIC-Spain)

12.20 - 12.40

C18: Energy integration and hydrodynamic characterization of dual CFB for sorption looping cycles; Luis Miguel Romeo (CIRCE-Spain)

12.40 - 13.00

C19: Improving efficiency of high temperature looping capture; Mike Haines (IEA GHG)

13.00 - 14.00 Lunch at INCAR-CSIC

Technical Session 5 : Performance of Solid Materials (II)

14.00 - 14.15

C20: Flame-made Ca-based nanosorbents with high CO2 uptake efficiency; Peter Smirniotis (University of Cincinnati-USA)

14.15 - 14.30

C21: Calcium Precursors to Produce CaO Sorbents for Multi-cycle CO2 Capture; Wenqiang Liu (University of Queensland-Australia)

14.30 - 14.45

C22: Attrition in fluidised bed systems; Ben Schüppel (Rheinkalk/lhoist -Germany) - Please email for password to open

14.45 - 15.00

C23: Need for standardisation of test methods for sorbent/material characterisation; Ulrich Zuberbühler (ZSW-Germany)

15.00 - 15.15

C24: CO2 Capture Capacity of CaO in Long Series of Pressure Swing Absorption Cycles; James Butler (University of British Columbia-Canada) et al

15.15 - 15.30

C25: Sorbent Particle Size Change and Steam Reactivation; Yinghai Wu (CANMET/Imperial College-UK/Canada)

15.30 - 15.45

C26: An Attrition-free Reactivation of Lime via Hydration; Vlatko Materic (Industrial Research Limited-New Zealand), Rob Holt

15.45 - 16.00

Discussion

16.00 - 16.30 Coffee Break

Technical Session 6 : Precombustion Ca-Looping (II)

16.30 - 16.50

C27: Calcium looping process for clean fossil fuel conversion; L.S. Fan/ Shwetha Ramkuma (The Ohio State University-USA)

16.50 - 17.10

C28: High capacity hydrotalcites; P.D. Cobden (ECN-Netherlands)

17.10 - 17.30

C29: Redox looping of supported Nickel catalyst during unmixed steam reforming of waste vegetable oil; Valerie Dupont (University of Leeds-UK) et al

17.30 - 17.50

C30: Circulating fluidized bed reactor for Sorption-Enhanced Methane Steam Reforming; Richard Blom/Bjørnard Arstad (SINTEF-Norway)

20.00 Dinner in Oviedo

 

Day 3 -Thursday 17th September

Technical Session 7 : Chemical Looping Combustion

09.00 - 09.20

C31: Chemical looping combustion of petroleum coke with Co-based oxygen carrier; Cai Ningsheng (Tsinghua University-China) et al

09.20 - 09.40

C32: Chemical-looping combustion and reforming at a 120 kW pilot plant - results using a nickel-based oxygen carrier; Tobias Proell (TUV-Austria)

09.40 - 10.00

C33: Carbon dioxide capture and subsequent water splitting for hydrogen production using a chemical looping process with a perovskite-type mixed conducting ceramic as oxygen carrier; Alan Thursfield (Newcastle University-UK) et al

10.00 - 10.20

C34: Effect of fuel gas composition (sulfur and light hydrocarbons) in Chemical-Looping combustion processes; Alberto Abad (ICB/CSIC-Spain) et al

10.30 - 11.00 Coffee Break

Technical Session 8 : Overviews

11.00 - 11.20

C35: Process simulation activities at Politecnico di Milano on Ca-based solid looping cycles; Matteo Romano (Politecnico di Milano-Italy)

11.20 - 11.40

C36: CO2 Capture Research at Cranfield University; J.E. Okey (Cranfield University-UK)

11.40 - 12.00

C37: Some Aspects of Calcium Looping Research at Imperial College, London; Paul Fennell (Imperial College-UK)

12.00 - 12.20

C38: Overview of ICB-CSIC activities in chemical looping combustion and reforming; Francisco Labiano (ICB/CSIC-Spain)

12.20 - 13.30

Summary and Future Network Actions (Steering Group)

13.30 - 14.30 Lunch at INCAR-CSIC

The Scientific committe for the Network will organise and manage the technical sessions

  • Mike Haines, IEA GHG
  • Douglas P. Harrison, Louisiana Sate University
  • Tobias Proell, Technical Univeristy of Wien
  • Paul S. Fennell, Imperial College
  • Edward J. Anthony, CANMET
  • Andrés Sanchez, ENDESA
  • Juan Carlos Abanades, INCAR-CSIC

 

 

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3. Travel and Hotel information

Rooms have been block booked in the hotels listed below; late reservations is still possible but the discounted room rates given no longer apply. Please mention in your reservation that you are attending a meeting at INCAR. September is a busy congress time in Oviedo.

Hotel Fruela
http://www.hotelfruela.com/
 80 € (breakfast included) + 7% VAT

AC Forum
http://www.ac-hotels.com/138-AC_OVIEDO_FORUM.html
90€ (breakfast not included + 7%VAT

HOTEL TRYP OVIEDO:

http://es.solmelia.com/hotel/tryp-oviedo.htm?idPrm=BUS002&idONg=REG&idNom=
GeneralOviedo&utm_source=BUS002&utm_
medium=cpc&utm_content=REG&utm_campaign=Oviedo
105 € (breakfast included) + 7% VAT

Hotel NH Principado
http://www.nh-hoteles.es/nh/es/hoteles/espana/oviedo/nh-principado.html
10 rooms 110 € (breakfast not included) + 7% VAT

Hotel Libretto
http://www.librettohotel.com/
Bed and Breakfast
€80 + 7% IVA  (double room)
€75 + 7% IVA  (single room)

Hotel M:
http://www.mhotel.es/
Bed and Breakfast
€80 + 7% IVA (double room)
€75 + 7% IVA  (single room)

Transport to INCAR

(located about 4 km from the center of Oviedo) can be done by train ("Renfe-Cercanias") or by bus (lines 2 y 12) (see http://www.incar.csic.es/pre07.php)

Direct link to Google maps of INCAR



 

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6. Registration

Payment of the registration fee (150 and 80 for students) needs to be made at the time of registration by either Mastercard or Visa.

Two working lunches, one evening reception (“vino español”) and one Network dinner are included in the registration fee.  Accomodation and transport costs are to be arranged individually by the participants.

Cancellation Policy

Cancellations are subject to a charge of €10

 

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Links:

Last meeting

 

 

Key Findings and Proposals

Below is a brief summary of key findings and proposals for the direction of further research and co-operation following the 1st meeting of the network. The meeting was attended by 77 people with a strong representation and interest from industry. It was agreed at the meeting that the next network meeting will be hosted by ECN of the Netherlands in the week before the GHGT-10 conference which is being held in Amsterdam in September 2010. More information about the the next meeting will be published shortly.

What we have learned

At least two new pilot demonstrations in the MW class are to be implemented in Spain (la Pereda for Ca-Looping) and Germany (Darmstadt, for CLC and Ca-looping) before 2010.

There are several small dual bed systems in operation at various research centres in the 10s kW scale range for CLC and Ca-looping. Extended operation of these rigs is important to gain design data and confidence in the technology, but there may be a danger of some duplication of activities.

New process variants of the basic CaO looping cycle are possible and more may be found.

Attrition is not the problem previously thought in some Ca-based systems.

Some groups are also examining pelletization strategies, and believe that they could make synthetic materials which are both relatively cheap, durable and have excellent long term carrying capacity

Both bubbling and entrained beds have been shown to work successfully in the solid looping application.

Make up rates of CaO can be reduced to very low levels

There is potential advantage for combining Chemical Looping Combustion and CO2 removal and significant advantages might result.

Nano particles of CaO eliminate the degradation process. They have to be deposited on a support and remain apart from one another to avoid sintering

Mixing nano particles with another substance can do the same but this time the nano particles of CaO are separated by particles of the second substance. As little as 18% of second material is sufficient.

Hydration of calcined material by different means, including some innovative contacting devices, can restore carbonation capacity. Exposing hydrated material to a CO2 atmosphere enables hydrated material to be heated above the dehydration point and further enhances the effects of reactivation by hydration. No noticeable reaction with CO2 is observed at temperatures up to 540C which is well above the normal decomposition temperature for the hydrate, an observation which has yet to be duplicated and further researched.

Mixed metal perovskites and similar compounds which can contain variable amounts of oxygen in the lattice are potential candidates for CLC processes.

A three step process including a hydration step has been operated at pilot scale.

It has been demonstrated that chemical looping combustion can be arranged so that free oxygen gas is made available for reaction in the fuel reactor thus enabling solid materials to be combusted using the “CLOU“ principle. (Chemical looping with Oxygen Uncoupling)

In chemical looping reforming systems it has been shown that all of the oxygen can be removed from the feed air if operating temperature is >900C.

It still seems to be difficult to reach 100% oxidation of fuel in fuel reactors in CLC systems

Sulphur affects metal oxides in CLC systems but sulphur can be more or less completely released in the air reactor if the supply of sulphur contaminated fuel is stopped for long enough.

Under pressurised conditions it is possible to fully desulphurise product (to <1ppm) in a sorption enhanced gasification and watergas shift process.


What we could do

Test various hydration schemes in small pilot plants in continuous mode

Develop alternative equipment for transferring solids between pressure levels

Test use of spent sorbent to remove sulphur compounds upstream of CaO absorption systems

Test novel sorbents which have increased resistance to chemical and mechanical degradation.

Minimise the duplication of pilot scale and demonstration scale testing programmes (but not so far that adequate verification/confirmation of findings is affected)

Develop equipment scale up capabilities through validated reactor and system models.

Exchange Register

It is proposed to post details of organisations who are:-

- Seeking testing/ development/ demonstration services
- Offering testing/ development/ demonstration services
- Seeking temporary placements for their researchers
- Offering temporary placements for other researchers
- Seeking exchange placements for their researchers

in the field of high temperature solid looping systems.

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Report of the meeting:
Available after the meeting

 

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Contact details:

For further information please contact Carlos Abanades,
abanades@incar.csic.es or Mike Haines mike@ieaghg.org

Queries regarding registration should be made to Andrea Lacey (andrea@ieaghg.org)


Back to High temperature solid looping cycles network page