o.mohammed@engslminerals.com Company profile (PDF)
Tall grey process columns and ducting beside red steel pipe racks at a chemical processing plant on a bright overcast day

Carbon capture and soda ash technology

Our process captures carbon dioxide from industrial flue gas and converts it into soda ash. It is described in international patent application WO2015194963A1.

The process

ENGSL has developed a process, known as Xeo-Light, that captures carbon dioxide from industrial flue gas and converts it into soda ash (sodium carbonate, Na₂CO₃).

The aim is to give an emitter a product it can sell, instead of a gas that has to be compressed and stored. Development began in 2007 with partners in Norway and China. Pilot work with the Masdar Institute in Abu Dhabi followed in 2018–2020.

The process also produces precipitated calcium carbonate (PCC) as a co-product. The patent application covers soda ash only.

Patent application

Number
WO2015194963A1
Type
International (PCT) patent application
Title
Process for producing soda ash
Applicants
ENGSL Minerals DMCC and EnPro
Inventor
Mohammed Olfi
Filed
18 June 2014
Published
23 December 2015

How the process works

Steps 1 and 2 are the two steps set out in the patent application. Its claims include CO₂ conversion above 90% and energy use of no more than 2.86 MWh per tonne of soda ash. The application describes this as at least 24% lower than the conventional Solvay process.

  1. Electrolysis

    Salt brine (sodium chloride) is electrolysed in an ion-exchange membrane cell to produce sodium hydroxide.

  2. Capture and reaction

    Flue gas passes through a packed column, where its CO₂ reacts with the sodium hydroxide.

  3. Crystallisation

    Soda ash (sodium carbonate) is crystallised and recovered from the solution.

  4. Products

    The recovered soda ash can be sold as an industrial product.

Public records

Patent documents, an engineering announcement and research relating to the technology, each with a link to its source.

Public records relating to ENGSL's carbon capture and soda ash technology, in date order
DateSourceWhat it records
2014–2015 WO2015194963A1 on Google Patents International patent application by ENGSL Minerals DMCC and EnPro, filed 18 June 2014 and published 23 December 2015.
29 January 2015 Pöyry press release Pöyry, now AFRY, was awarded basic engineering services by EnPro AS for a planned soda ash plant at Kollsnes, Norway. The release names ENGSL Minerals DMCC as EnPro's technology cooperation partner.
6 May 2015 EP2558185B1 on Google Patents Earlier related European patent (application WO2011129707A1), “CO₂ scrubber/separator using a cyclic carbonator for controlled carbonate/bicarbonate production”. Applicants Engineering Solutions Ltd and EnPro AS; inventors Olfi Mohamed and Tarek R. Farhat. Granted 6 May 2015; no longer in force.
31 May 2016 Masdar Institute news release Techno-economic analysis of the technology by a Masdar Institute team led by Dr Mohammad Abu Zahra. It names ENGSL Minerals DMCC as EnPro's technology partner. The Masdar Institute is now part of Khalifa University. The study's estimates are set out below.
2019 Journal of Cleaner Production Peer-reviewed techno-economic comparison of soda ash production with monoethanolamine (MEA) scrubbing for power-plant CO₂. It reported a capital cost for the soda ash route of about 65% of that of the MEA process. Khalifa University lists ENGSL among the affiliated organisations.

Masdar Institute study, 2016

The study modelled the process for a 560 MW natural gas-fired power plant in the UAE and compared it with amine-based carbon capture.

The figures are modelled study estimates. They are not measured plant performance.

CO₂ captured
Could capture up to 1.3 million tonnes a year, about 85% of the plant's CO₂
Capital cost
Could be up to 35% lower than amine-based capture
Energy demand
Could be up to 65% lower than amine-based capture
Soda ash sales
Capture costs could be offset by selling soda ash for a minimum of US$18 per ton. The release notes that soda ash had sold for more than US$200 per ton.

Development history

Stages in the development of the technology, as recorded by ENGSL.

Development history of the technology
PeriodLocationActivityBasis
2007–2008 Norway Carbon capture system for EnPro Norway: supply, installation, commissioning and operations management. Company records
2007–2011 Partners in China and Norway Pilot plant construction and patent filing. Collaboration with Tsinghua University, Beijing, on absorption–desorption facility technology, and with Statoil Hydro, Norway. Company records
2018–2020 UAE Xeo-Light carbon capture pilot with the Masdar Institute of Technology, Abu Dhabi: pilot plant design, optimisation, testing and validation under Middle East climatic and operating conditions. Company records
2019–2021 UAE Xeo-Light commercial soda ash plant using captured CO₂: engineering, procurement, construction, commissioning, start-up and operational handover. Company records

Working with ENGSL on the technology

We discuss the technology with companies that have a CO₂ source or plan a soda ash plant. For a first discussion, tell us the type of CO₂ source, the flue-gas volume if known, and the kind of collaboration you have in mind.

  • Technology licensing
  • Joint venture discussions
  • Carbon capture deployment studies for a specific CO₂ source
  • Soda ash plant development

Discuss a carbon capture application

Our team in Dubai will review your enquiry and reply by email.

Make an enquiry