Carbon capture and storage

Schematic showing both terrestrial and geological sequestration of carbon dioxide emissions from a coal-fired plant

Carbon capture and storage (CCS) (or carbon capture and sequestration) is the process of capturing waste carbon dioxide (CO₂) from large point sources, such as fossil fuel power plants, transporting it to a storage site, and depositing it where it will not enter the atmosphere, normally an underground geological formation. The aim is to prevent the release of large quantities of CO₂ into the atmosphere (from fossil fuel use in power generation and other industries). It is a potential means of mitigating the contribution of fossil fuel emissions to global warming^[1] and ocean acidification.^[2] Although CO₂ has been injected into geological formations for several decades for various purposes, including enhanced oil recovery, the long term storage of CO₂ is a relatively new concept. The first commercial example was the Weyburn-Midale Carbon Dioxide Project in 2000.^[3] Other examples include SaskPower's Boundary Dam and Mississippi Power's Kemper Project. 'CCS' can also be used to describe the scrubbing of CO₂ from ambient air as a climate engineering technique.

An integrated pilot-scale CCS power plant was to begin operating in September 2008 in the eastern German power plant Schwarze Pumpe run by utility Vattenfall, to test the technological feasibility and economic efficiency. CCS applied to a modern conventional power plant could reduce CO₂ emissions to the atmosphere by approximately 80–90% compared to a plant without CCS.^[4] The IPCC estimates that the economic potential of CCS could be between 10% and 55% of the total carbon mitigation effort until year 2100.^[4]

Carbon Dioxide can be captured out of air or fossil fuel power plant flue gas using absorption (or carbon scrubbing), membrane gas separation, or adsorption technologies. Amines are the leading carbon scrubbing technology. Capturing and compressing CO₂ may increase the energy needs of a coal-fired CCS plant by 25–40%.^[4] These and other system costs are estimated to increase the cost per Watt energy produced by 21–91% for fossil fuel power plants. ^[4] Applying the technology to existing plants would be more expensive, especially if they are far from a sequestration site. However, recent industry reports suggest that with successful research, development and deployment (RD&D), sequestered coal-based electricity generation in 2025 may cost less than unsequestered coal-based electricity generation today. ^[5]

Storage of the CO₂ is envisaged either in deep geological formations, or in the form of mineral carbonates. Deep ocean storage is not currently considered feasible due to the associated effect of ocean acidification.^[6] Geological formations are currently considered the most promising sequestration sites. The National Energy Technology Laboratory (NETL) reported that North America has enough storage capacity for more than 900 years worth of carbon dioxide at current production rates.^[7] A general problem is that long term predictions about submarine or underground storage security are very difficult and uncertain, and there is still the risk that CO₂ might leak into the atmosphere.^[8]

Capture

Capturing CO₂ is most effective at point sources, such as large fossil fuel or biomass energy facilities, industries with major CO₂ emissions, natural gas processing, synthetic fuel plants and fossil fuel-based hydrogen production plants. Extracting CO₂ from air is also possible, but not very practical because the CO₂ is not concentrated. ^[9]

Flue gas from the combustion of coal in oxygen has a large concentration of CO2, about 10-15% CO₂ whereas natural gas power plant flue gas is about 5-10% CO₂ ^[10]. Therefore, it is more energy and cost efficient to capture CO2 from coal-fired power plants. Impurities in CO₂ streams, like sulfurs and water, could have a significant effect on their phase behaviour and could pose a significant threat of increased corrosion of pipeline and well materials.[10] In instances where CO₂ impurities exist, especially with air capture, a scrubbing separation process would be needed to initially clean the flue gas. ^[11] According to the Wallula Energy Resource Center in Washington state, by gasifying coal, it is possible to capture approximately 65% of carbon dioxide embedded in it and sequester it in a solid form. ^[12]

Broadly, three different configurations of technologies for capture exist: post-combustion, pre-combustion, and oxyfuel combustion:

• In post combustion capture, the CO₂ is removed after combustion of the fossil fuel — this is the scheme that would be applied to fossil-fuel burning power plants. Here, carbon dioxide is captured from flue gases at power stations or other large point sources. The technology is well understood and is currently used in other industrial applications, although not at the same scale as might be required in a commercial scale power station. Post combustion capture is most popular in research because existing fossil fuel power plants can be retrofitted to include CCS technology in this configuration. ^[13]
• The technology for pre-combustion is widely applied in fertilizer, chemical, gaseous fuel (H₂, CH₄), and power production.^[14] In these cases, the fossil fuel is partially oxidized, for instance in a gasifier. The resulting syngas (CO and H₂) is shifted into CO₂ and H₂. The resulting CO₂ can be captured from a relatively pure exhaust stream. The H₂ can now be used as fuel; the carbon dioxide is removed before combustion takes place. There are several advantages and disadvantages when compared to conventional post combustion carbon dioxide capture.^[15][16] The CO₂ is removed after combustion of fossil fuels, but before the flue gas is expanded to atmospheric pressure. This scheme is applied to new fossil fuel burning power plants, or to existing plants where re-powering is an option. The capture before expansion, i.e. from pressurized gas, is standard in almost all industrial CO₂ capture processes, at the same scale as will be required for utility power plants.^[17][18]
• In oxy-fuel combustion^[19] the fuel is burned in oxygen instead of air. To limit the resulting flame temperatures to levels common during conventional combustion, cooled flue gas is recirculated and injected into the combustion chamber. The flue gas consists of mainly carbon dioxide and water vapour, the latter of which is condensed through cooling. The result is an almost pure carbon dioxide stream that can be transported to the sequestration site and stored. Power plant processes based on oxyfuel combustion are sometimes referred to as "zero emission" cycles, because the CO₂ stored is not a fraction removed from the flue gas stream (as in the cases of pre- and post-combustion capture) but the flue gas stream itself. A certain fraction of the CO₂ generated during combustion will inevitably end up in the condensed water. To warrant the label "zero emission" the water would thus have to be treated or disposed of appropriately. The technique is promising, but the initial air separation step demands a lot of energy.

Capture Technologies

Carbon dioxide can be separated out of air or flue gas with absorption, adsorption, or membrane gas separation technologies. Absorption, or carbon scrubbing, with amines is currently the dominant capture technology. Membrane and adsorption technologies are still in the developmental research stages, initiating primary pilot plants in the near future. Metal-Organic Frameworks (MOFs) are a novel, promising adsorption carbon capture technology.

Carbon dioxide adsorbs to a MOF through physisorption or chemisorption based on the porosity and selectivity of the MOF leaving behind a Greenhouse gas poor gas stream that is more environmentally friendly. The carbon dioxide is then stripped off the MOF using temperature swing adsorption (TSA) or pressure swing adsorption (PSA) so the MOF can be reused. Adsorbents and absorbents require regeneration steps where the CO₂ is removed from the sorbent or solution that collected it out of the flue gas in order for the sorbent or solution to be reused. Monoethanolamine (MEA) solutions, the leading amine for capturing CO₂, have a heat capacity between 3-4 J/g K since they are mostly water. ^{[20] [21]} Higher heat capacities add to the energy penalty in the solvent regeneration step. Thus, to optimize a MOF for carbon capture, low heat capacities and heats of adsorption are desired. Additionally, high working capacity and high selectivity are selected for in order to capture as much CO₂ as possible from the flue gas. However, there is an energy trade off with selectivity and energy expenditure. ^[22] As the amount of CO₂ captured increases, the energy, and therefore cost, required to regenerate increases. A large drawback of MOFs for CCS is their chemical and thermal stability. ^[23] Current research is looking to optimize MOF properties for CCS, but it has proven difficult to find these optimizations that also result in a stable MOF. Metal reservoirs are also a limiting factor to the potential success of MOFs. ^[24]

Capture is attributed to about two thirds of the total cost of CCS, making it limit the wide-scale deployment of CCS technologies. To optimize a CO₂ capture process would significantly increase the feasibility of CCS since the transport and storage steps of CCS are rather mature technologies. ^[25]

Organisms that produce ethanol by fermentation generate cool, essentially pure CO₂ that can be pumped underground.^[26] Fermentation produces slightly less CO₂ than ethanol by weight.

An alternate method under development is chemical looping combustion (CLC). Chemical looping uses a metal oxide as a solid oxygen carrier. Metal oxide particles react with a solid, liquid or gaseous fuel in a fluidized bed combustor, producing solid metal particles and a mixture of carbon dioxide and water vapor. The water vapor is condensed, leaving pure carbon dioxide, which can then be sequestered. The solid metal particles are circulated to another fluidized bed where they react with air, producing heat and regenerating metal oxide particles that are recirculated to the fluidized bed combustor. A variant of chemical looping is calcium looping, which uses the alternating carbonation and then calcination of a calcium oxide based carrier as a means of capturing CO₂.^[27]

A few engineering proposals have been made for the more difficult task of removing CO₂ from the atmosphere – a form of climate engineering – but work in this area is still in its infancy. Capture costs are estimated to be higher than from point sources, but may be feasible for dealing with emissions from diffuse sources such as automobiles and aircraft.^[28] The theoretically required energy for air capture is only slightly more than for capture from point sources. The additional costs come from the devices that use the natural air flow. Global Research Technologies demonstrated a pre-prototype of air capture technology in 2007.^[29]

Transport

After capture, the CO₂ would have to be transported to suitable storage sites. This would most likely be done by pipeline, which is generally the cheapest form of transport. In 2008, there were approximately 5,800 km of CO₂ pipelines in the United States, used to transport CO₂ to oil production fields where it is then injected into older fields to extract oil. The injection of CO₂ to produce oil is generally called Enhanced Oil Recovery or EOR. In addition, there are several pilot programs in various stages to test the long-term storage of CO₂ in non-oil producing geologic formations.

According to the Congressional Research Service, "There are important unanswered questions about pipeline network requirements, economic regulation, utility cost recovery, regulatory classification of CO₂ itself, and pipeline safety. Furthermore, because CO₂ pipelines for enhanced oil recovery are already in use today, policy decisions affecting CO₂ pipelines take on an urgency that is unrecognized by many. Federal classification of CO₂ as both a commodity (by the Bureau of Land Management) and as a pollutant (by the Environmental Protection Agency) could potentially create an immediate conflict which may need to be addressed not only for the sake of future CCS implementation, but also to ensure consistency of future CCS with CO₂ pipeline operations today."^[30][31]

Ships could also be utilized for transport where pipelines are not feasible. These methods are currently used for transporting CO₂ for other applications.

Sequestration

Various forms have been conceived for permanent storage of CO₂. These forms include gaseous storage in various deep geological formations (including saline formations and exhausted gas fields), and solid storage by reaction of CO₂ with metal oxides to produce stable carbonates.

Geological storage

Also known as geo-sequestration, this method involves injecting carbon dioxide, generally in supercritical form, directly into underground geological formations. Oil fields, gas fields, saline formations, unmineable coal seams, and saline-filled basalt formations have been suggested as storage sites. Various physical (e.g., highly impermeable caprock) and geochemical trapping mechanisms would prevent the CO₂ from escaping to the surface.^[32]

CO₂ is sometimes injected into declining oil fields to increase oil recovery. Approximately 30 to 50 million metric tonnes of CO₂ are injected annually in the United States into declining oil fields.^[33] This option is attractive because the geology of hydrocarbon reservoirs is generally well understood and storage costs may be partly offset by the sale of additional oil that is recovered.^[34] Disadvantages of old oil fields are their geographic distribution and their limited capacity, as well as the fact that subsequent burning of the additional oil recovered will offset much or all of the reduction in CO₂ emissions.^[35]

Unmineable coal seams can be used to store CO₂ because the CO₂ molecules attach to the surface of coal. The technical feasibility, however, depends on the permeability of the coal bed. In the process of absorption the coal releases previously absorbed methane, and the methane can be recovered (enhanced coal bed methane recovery). The sale of the methane can be used to offset a portion of the cost of the CO₂ storage. Burning the resultant methane, however, would negate some of the benefit of sequestering the original CO₂.

Saline formations contain highly mineralized brines, and have so far been considered of no benefit to humans. Saline aquifers have been used for storage of chemical waste in a few cases. The main advantage of saline aquifers is their large potential storage volume and their common occurrence. The major disadvantage of saline aquifers is that relatively little is known about them, especially compared to oil fields. To keep the cost of storage acceptable, the geophysical exploration may be limited, resulting in larger uncertainty about the aquifer structure. Unlike storage in oil fields or coal beds, no side product will offset the storage cost. Leakage of CO₂ back into the atmosphere may be a problem in saline aquifer storage. Current research shows, however, that trapping mechanisms such as structural trapping, residual trapping, solubility trapping and mineral trapping could immobilize the CO₂ underground and reduce the risk of leakage.^[32]

Enhanced oil recovery

Enhanced oil recovery (EOR) is a generic term for techniques used to increase the amount of crude oil that can be extracted from an oil field. In Carbon Capture & Sequestration Enhanced Oil Recovery (CCS EOR), carbon dioxide is injected into an oil field to recover oil that is often never recovered using more traditional methods.

Crude oil development and production in U.S. oil reservoirs can include up to three distinct phases: primary, secondary, and tertiary (or enhanced) recovery.^[36] During primary recovery only about 10 percent of a reservoir's original oil in place is typically produced. Secondary recovery techniques extend a field's productive life generally by injecting water or gas to displace oil and drive it to a production wellbore, resulting in the recovery of 20 to 40 percent of the original oil in place. However, with much of the easy-to-produce oil already recovered from U.S. oil fields, producers have attempted several tertiary, or enhanced oil recovery (EOR), techniques that offer prospects for ultimately producing 30 to 60 percent, or more, of the reservoir's original oil in place.^[37]

An example of a project that will use CCS EOR is the Kemper Project in Mississippi. Due to the Kemper Project's close proximity to oil fields, the carbon dioxide byproduct from producing electricity will be transported to the neighboring oil fields for EOR.^[38]

Ocean storage

In the past, it was suggested that CO₂ could be stored in the oceans, but this would only exacerbate ocean acidification and has been made illegal under specific regulations. Ocean storage is no longer considered feasible.^[6]

Mineral storage

In this process, CO₂ is exothermically reacted with available metal oxides, which in turn produces stable carbonates (e.g. calcite, magnesite). This process occurs naturally over many years and is responsible for a great amount of surface limestone. The idea of using olivine has been promoted by the geochemist Prof. Schuiling.^[39] The reaction rate can be made faster, for example, with a catalyst^[40] or by reacting at higher temperatures and/or pressures, or by pre-treatment of the minerals, although this method can require additional energy. The IPCC estimates that a power plant equipped with CCS using mineral storage will need 60–180% more energy than a power plant without CCS.^[4]

The economics of mineral carbonation at scale are now being tested in a world-first pilot plant project based in Newcastle, Australia. New techniques for mineral activation and reaction have been developed the GreenMag Group and the University of Newcastle and funded by the New South Wales and Australian Governments to be operational by 2013.^[41]

In 2009 it was reported that scientists had mapped 6,000 square miles (16,000 km²) of rock formations in the U.S. that could be used to store 500 years' worth of U.S. carbon dioxide emissions.^[42] A study on mineral sequestration in the US states:

Carbon sequestration by reacting naturally occurring Mg and Ca containing minerals with CO₂ to form carbonates has many unique advantages. Most notabl[e] is the fact that carbonates have a lower energy state than CO₂, which is why mineral carbonation is thermodynamically favorable and occurs naturally (e.g., the weathering of rock over geologic time periods). Secondly, the raw materials such as magnesium based minerals are abundant. Finally, the produced carbonates are unarguably stable and thus re-release of CO₂ into the atmosphere is not an issue. However, conventional carbonation pathways are slow under ambient temperatures and pressures. The significant challenge being addressed by this effort is to identify an industrially and environmentally viable carbonation route that will allow mineral sequestration to be implemented with acceptable economics.^[43]

The following table lists principal metal oxides of Earth's Crust. Theoretically, up to 22% of this mineral mass is able to form carbonates.

Earthen Oxide	Percent of Crust	Carbonate	Enthalpy change (kJ/mol)
SiO2	59.71
Al2O3	15.41
CaO	4.90	CaCO3	-179
MgO	4.36	MgCO3	-118
Na2O	3.55	Na2CO3	-322
FeO	3.52	FeCO3	-85
K2O	2.80	K2CO3	-393.5
Fe2O3	2.63	FeCO3	112
	21.76	All Carbonates

Ultramafic mine tailings are a readily available source of fine-grained metal oxides that can act as artificial carbon sinks to reduce net greenhouse gas emissions in the mining industry.^[44] Accelerating passive CO₂ sequestration via mineral carbonation may be achieved through microbial processes that enhance mineral dissolution and carbonate precipitation.^[45][46][47]

Energy requirements

The energy requirements of sequestration processes may be significant. In one paper, sequestration consumed 25 percent of the plant's rated 600-megawatt output capacity.^[48]

After adding CO₂ capture and compression, the capacity of the coal-fired power plant is reduced to 457 MW.

Leakage

Lake Nyos as it appeared fewer than two weeks after the eruption; August 29, 1986.

A major concern with CCS is whether leakage of stored CO₂ will compromise CCS as a climate change mitigation option. For well-selected, designed and managed geological storage sites, IPCC estimates that risks are comparable to those associated with current hydrocarbon activity.^[49] However, this finding is contested due to a lack of experience in such long term storage.^[50][51] CO₂ could be trapped for millions of years, and although some leakage occurs upwards through the soil, well selected storage sites are likely to retain over 99% of the injected CO₂ over 1000 years.^[52] Leakage through the injection pipe is a greater risk.^[53]

Although the injection pipe is usually protected with non-return valves to prevent release on a power outage, there is still a risk that the pipe itself could tear and leak due to the pressure. The Berkel en Rodenrijs incident in December 2008 was an example, where a modest release of CO₂ from a pipeline under a bridge resulted in the deaths of some ducks sheltering there.^[54] In order to measure accidental carbon releases more accurately and decrease the risk of fatalities through this type of leakage, the implementation of CO₂ alert meters around the project perimeter has been proposed. Malfunction of a carbon dioxide industrial fire suppression system in a large warehouse released CO₂ and 14 citizens collapsed on the nearby public road. A release of CO₂ from a salt mine killed a person at distance of 300 meters.^[55]

In 1986 a large leakage of naturally sequestered CO₂ rose from Lake Nyos in Cameroon and asphyxiated 1,700 people. While the carbon had been sequestered naturally, some point to the event as evidence for the potentially catastrophic effects of sequestering carbon artificially.^[56] The Lake Nyos disaster resulted from a volcanic event, which very suddenly released as much as a cubic kilometre of CO₂ gas from a pool of naturally occurring CO₂ under the lake in a deep narrow valley. The location of this pool of CO₂ is not a place where man can inject or store CO₂, and this pool was not known about nor monitored until after the occurrence of the natural disaster.

For ocean storage, the retention of CO₂ would depend on the depth. The IPCC estimates 30–85% of the sequestered carbon dioxide would be retained after 500 years for depths 1000–3000 m. Mineral storage is not regarded as having any risks of leakage. The IPCC recommends that limits be set to the amount of leakage that can take place. This might rule out deep ocean storage as an option.

At the conditions of the deeper oceans, (about 400 bar or 40 MPa, 280 K) water–CO₂(l) mixing is very low (where carbonate formation/acidification is the rate limiting step), but the formation of water-CO₂ hydrates, a kind of solid water cage that surrounds the CO₂, is favorable.

To further investigate the safety of CO₂ sequestration, Norway's Sleipner gas field can be studied, as it is the oldest plant that stores CO₂ on an industrial scale. According to an environmental assessment of the gas field which was conducted after ten years of operation, the author affirmed that geosequestration of CO₂ was the most definite form of permanent geological storage of CO₂:

Available geological information shows absence of major tectonic events after the deposition of the Utsira formation [saline reservoir]. This implies that the geological environment is tectonically stable and a site suitable for carbon dioxide storage. The solubility trapping [is] the most permanent and secure form of geological storage.^[57]

In March 2009 StatoilHydro issued a study showing the slow spread of CO₂ in the formation after more than 10 years operation.^[58]

Phase I of the Weyburn-Midale Carbon Dioxide Project in Weyburn, Saskatchewan, Canada has determined that the likelihood of stored CO₂ release is less than one percent in 5,000 years.^[59] A January 2011 report, however, claimed evidence of leakage in land above that project.^[60] This report was strongly refuted by the IEAGHG Weyburn-Midale CO₂ Monitoring and Storage Project, which issued an eight-page analysis of the study, claiming that it showed no evidence of leakage from the reservoir.^[61]

The liability of potential leak(s) is one of the largest barriers to large-scale CCS. To assess and reduce such liability, the leakage of stored gasses, particularly carbon dioxide, into the atmosphere may be detected via atmospheric gas monitoring, and can be quantified directly via the eddy covariance flux measurements,^[62][63][64]

Carbon dioxide recycling - carbon capture and utilization (CCU)

Recycling CO₂ may offer a response to the global challenge of significantly reducing greenhouse gas emissions from major stationary (industrial) emitters in the near to medium term, but is usually considered a different technological category from CCS.^[65] Technologies under development, such as Bio CCS Algal Synthesis,^[66] utilises pre-smokestack CO₂ (such as from a coal-fired power station) as a useful feedstock input to the production of oil-rich algae in solar membranes to produce oil for plastics and transport fuel (including aviation fuel), and nutritious stock-feed for farm animal production.^[66] The CO₂ and other captured greenhouse gases are injected into the membranes containing waste water and select strains of algae causing, together with sunlight or UV light, an oil rich biomass that doubles in mass every 24 hours.

The Bio CCS Algal Synthesis process is based on earth science photosynthesis: the technology is entirely retrofittable and collocated with the emitter, and the capital outlays may offer a return upon investment due to the high value commodities produced (oil for plastics, fuel and feed).

Bio CCS Algal Synthesis test facilities are being trialed at Australia's three largest coal-fired power stations (Tarong, Queensland; Eraring, NSW; Loy Yang, Victoria) using piped pre-emission smokestack CO₂ (and other greenhouse gases) as feedstock to grow oil-rich algal biomass in enclosed membranes for the production of plastics, transport fuel and nutritious animal feed.

Another potentially useful way of dealing with industrial sources of CO₂ is to convert it into hydrocarbons where it can be stored or reused as fuel or to make plastics. There are a number of projects investigating this possibility.^[67]

Carbon dioxide scrubbing variants exist based on potassium carbonate which can be used to create liquid fuels, though this process requires a great deal of energy input.^[68] Although the creation of fuel from atmospheric CO₂ is not a climate engineering technique, nor does it actually function as greenhouse gas remediation, it nevertheless is potentially useful in the creation of a low carbon economy.

Other uses are the production of stable carbonates from silicates (e.g. olivine produces Magnesium carbonate. This process is still in the R&D phase.^[69]

Single step methods: methanol

A proven process to produce a hydrocarbon is to make methanol. Methanol is rather easily synthesized from CO₂ and H₂ (See Green Methanol Synthesis). Based on this fact the idea of a methanol economy was born.

Single step methods: hydrocarbons

At the department of Industrial Chemistry and Engineering of Materials at the University of Messina, Italy, there is a project to develop a system which works like a fuel-cell in reverse, whereby a catalyst is used that enables sunlight to split water into hydrogen ions and oxygen gas. The ions cross a membrane where they react with the CO₂ to create hydrocarbons.^[70]

Two step methods

If CO₂ is heated to 2400 °C, it splits into carbon monoxide (CO) and oxygen. The Fischer-Tropsch process can then be used to convert the CO into hydrocarbons. The required temperature can be achieved by using a chamber containing a mirror to focus sunlight on the gas. Rival teams are developing such chambers, at Solarec and at Sandia National Laboratories, both based in New Mexico.^[71] According to Sandia these chambers could provide enough fuel to power 100% of domestic vehicles using 5800 km²; unlike biofuels this would not take fertile land away from crops but would be land that is not being used for anything else. James May, the British TV presenter, visited a demonstration plant in a programme in his 'Big Ideas' series.

Example CCS projects

Industrial-scale projects

As of September 2012, the Global CCS Institute identified 75 large-scale integrated projects in its 2012 Global Status of CCS report^[72] which is a net increase of one project since its 2011 Global Status of CCS report. 16 of these projects are in operation or in construction capturing around 36 million tonnes of CO₂ per annum.^[72][73] For more information see Integrated CCS Projects^[74] on the Global CCS Institute's website. For information on EU projects see Zero Emissions Platform^[75] website. The eight large-scale integrated CCS projects currently in operation are:

1. In Salah CO₂ Injection — Algeria

In Salah is a fully operational onshore gas field with CO₂ injection. CO₂ is separated from produced gas and reinjected in the producing hydrocarbon reservoir zones. Since 2004, about 1 Mt/a of CO₂ has been captured during natural gas extraction and injected into the Krechba geologic formation at a depth of 1,800m. The Krechba formation is expected to store 17Mt CO₂ over the life of the project.

Injection suspended in 2011 due to concerns about the integrity of the seal. https://sequestration.mit.edu/tools/projects/in_salah.html

As a precautionary measure, injection has been reduced by 15 to 20% pending the detailed conclusions from well data and seismic interpretation. http://www.statoil.com/AnnualReport2010/en/sustainability/Health,Safety,ClimateAndTheEnvironment/Climate/CarbonCaptureAndStorage/Pages/OurCCSProjects.aspx

2. Sleipner CO₂ Injection — Norway

Sleipner^[58] is a fully operational offshore gas field with CO₂ injection initiated in 1996. CO₂ is separated from produced gas and reinjected in the Utsira saline aquifer (800–1000 m below ocean floor) above the hydrocarbon reservoir zones. This aquifer extends much further north from the Sleipner facility at its southern extreme. The large size of the reservoir accounts for why 600 billion tonnes of CO₂ are expected to be stored, long after the Sleipner natural gas project has ended.

3. Snøhvit CO₂ Injection — Norway

Snøhvit is a fully operational offshore gas field with CO₂ injection. The LNG plant is located onshore. CO₂ is necessarily separated to produce liquefied natural gas (LNG) and then CO₂ is injected in a saline aquifer below the hydrocarbon reservoir zones offshore at a rate of 700,000 t/a into the Tubåen sandstone formation 2,600 m under the seabed for storage. This formation was closed April 2011, and injection started in the Stø-formation where produced gas is taken. Produced CO₂ is increasing, therefore separation capacity may limit production before end 2015 when a new formation will be drilled for CO₂-injection only. (Teknisk Ukeblad nr. 30, 2013, tu.no)

4. Great Plains Synfuel Plant and Weyburn-Midale Project — Canada

Weyburn-Midale is a coal gasification operation that produces synthetic natural gas and various petrochemicals from coal. This project captures about 2.8 Mt/a of CO₂ from its coal gasification plant located in North Dakota, US, transported by pipeline 320 km across the Canadian border and injects it into depleting oil fields in Saskatchewan where it is used for enhanced oil recovery (EOR).

5. Shute Creek Gas Processing Facility — US

Around 7 million tonnes per annum of carbon dioxide are recovered from ExxonMobil's Shute Creek gas processing plant in Wyoming, and transported by pipeline to various oil fields for enhanced oil recovery. This project has been operational since 1986.

6. Enid Fertilizer — US

The Enid Fertilizer plant sends 675,000 tonnes of CO₂ to be used for EOR. The pipeline and wells are operated separately by Anadarko Petroleum.

7. Val Verde Natural Gas Plants — US

CO₂ from Mitchell, Gray Ranch, Puckett, and Turrell gas processing plants is transported via the Val Verde and CRC pipelines for EOR (incl. Sharon Ridge EOR field).

8. Century Plant — US

Occidental Petroleum, along with Sandridge Energy, is operating a West Texas hydrocarbon gas processing plant and related pipeline infrastructure that provides CO₂ for use in EOR. With a total CO₂ capture capacity of 8.5 Mt/a expected in 2012, the Century plant would be the largest single industrial source CO₂ capture facility in North America.

9. Duke Energy East Bend Station — US

Researchers at the Center for Applied Energy Research of the University of Kentucky are currently developing the algae-mediated conversion of coal-fired power plant flue gas to drop-in hydrocarbon fuels. Through their work, these researchers have proven that the carbon dioxide within flue gas from coal-fired power plants can be captured using algae, which can be subsequently harvested and utilized, e.g. as a feedstock for the production of drop-in hydrocarbon fuels.^[76][77]

Canada

The federal government in the 2008 and 2009 budgets has invested approximately $1.4 billion in Carbon Capture and Storage development.^[78]

Alberta

Alberta has committed $170 million in 2013/2014 – and a total of $1.3 billion over 15 years – to fund two large-scale CCS projects that will help reduce CO₂ emissions from oil sands refining.^[79] In 2010 a grant agreement was signed with the Alberta Carbon Trunk Line.^[80] The second is the Quest Project.^[81] The Quest project uses amine absorption to capture CO₂ from the Scotford Steam Methane Reformer units. Approximately 1.2 Mtonne CO₂ per year is captured and transported through 64 km of onshore pipeline into a saline aquifer in the Cambrian Basal Sands.^[82]

British Columbia

Spectra Energy's Fort Nelson Project is proposed but still needs to secure funding.^[83] The total project cost is estimated to be US $12.5 Million. The source of CO₂ will be from the Fort Nelson Natural Gas Processing Plant and will be transported 15 km via an onshore pipeline to middle Devonian carbonate rock that is between 6500 and 7000 feet deep. The process will capture 2.2 Megatonne CO₂ per year using an amine process in its pre-combustion capture. Injections and MVA Operations have already occurred (2014) and is projected to startup in 2018.^[84]

Saskatchewan

Led by the province's full-service utility, SaskPower, one of the world's first and largest full production carbon capture facilities is operating at Boundary Dam Power Station. With an initial investment of $1.5 to $1.6 billion,^[85] SaskPower will be generating a revenue by selling a portion of the captured CO₂ back into the market to be used for enhanced oil recovery. The project started in May 2011 and became operational in October 2014.^[86] The post-combustion full flue gas capture process will capture 1 million tonnes of CO₂ a year.^[83]

Pilot projects

The Alberta Saline Aquifer Project (ASAP), Husky Upgrader and Ethanol Plant pilot, Heartland Area Redwater Project (HARP), Wabamun Area Sequestration Project(WASP), and Aquistore.^[87]

Another Canadian initiative is the Integrated CO₂ Network (ICO₂N), a group of industry participants providing a framework for carbon capture and storage development in Canada.^[88] Other Canadian organizations related to CCS include CCS 101, Carbon Management Canada, IPAC CO₂, and the Canadian Clean Power Coalition.^[89]

Netherlands

In the Netherlands, a 68-megawatt oxyfuel plant ("Zero Emission Power Plant") was being planned to be operational in 2009.^[90] This project was later canceled.

ROAD (Rotterdam Capture and Storage Demonstration project) is a joint project by E.ON Benelux and Electrabel Nederland / GDF SUEZ Group. Every year, starting in 2015 ROAD will capture around 1.1 million tonnes of CO₂ at the new power plant on the Maasvlakte. This will be stored in depleted gas reservoirs under the North Sea.^[91]

Developed in the Netherlands, an electrocatalysis by a copper complex helps reduce carbon dioxide to oxalic acid.^[92]

Norway

In Norway, the CO₂ Technology Centre (TCM) at Mongstad began construction in 2009, and completed in 2012. It includes two capture technology plants (one advanced amine and one chilled ammonia), both capturing fluegas from two sources. This includes a gas-fired power plant and refinery cracker fluegas (similar to coal-fired power plant fluegas).

In addition to this, the Mongstad site was also planned to have a full-scale CCS demonstration plant. The project was delayed to 2014, 2018, and then indefinitely.^[93] The project cost rose to USD 985 million.^[94] Then in October 2011, Aker Solutions' wrote off its investment in Aker Clean Carbon, declaring the carbon sequestration market to be "dead".^[95]

On 1 October 2013 Norway asked Gassnova not to sign any contracts for Carbon capture and storage outside Mongstad.^[96]

Poland

In Belchatów, Poland,^[97] a lignite-fired energy plant of more than 858 MW is planned to be in operation in 2013.^[98][99]

United States

In November 2008, the DOE awarded a $66.9 million eight-year grant to a research partnership headed by Montana State University to demonstrate that underground geologic formations "can store huge volumes of carbon dioxide economically, safely and permanently". Researchers under the Big Sky Regional Carbon Sequestration Project plan to inject up to one million tonnes of CO₂ into sandstone beneath southwestern Wyoming.^[100]

In the United States, four different synthetic fuel projects are moving forward, which have publicly announced plans to incorporate carbon capture and storage:

1. American Clean Coal Fuels, in their Illinois Clean Fuels (ICF) project, is developing a 30,000-barrel (4,800 m³) per day biomass and coal to liquids project in Oakland, Illinois, which will market the CO₂ created at the plant for enhanced oil recovery applications. By combining sequestration and biomass feedstocks, the ICF project will achieve dramatic reductions in the life-cycle carbon footprint of the fuels they produce. If sufficient biomass is used, the plant should have the capability to go life-cycle carbon negative, meaning that effectively, for each gallon of their fuel that is used, carbon is pulled out of the air, and put into the ground.^[101]
2. Baard Energy, in their Ohio River Clean Fuels project, is developing a 53,000 bbl/d (8,400 m³/d) coal and biomass to liquids project, which has announced plans to market the plant's CO₂ for enhanced oil recovery.^[102]
3. Rentech is developing a 29,600-barrel (4,710 m³) per day coal and biomass to liquids plant in Natchez, Mississippi, which will market the plant's CO₂ for enhanced oil recovery. The first phase of the project is expected in 2011.^[103]
4. DKRW is developing a 15,000–20,000-barrel (2,400–3,200 m³) per day coal to liquids plant in Medicine Bow, Wyoming, which will market its plant's CO₂ for enhanced oil recovery. The project is expected to begin operation in 2013.^[104]

In October 2009, the U.S. Department of Energy awarded grants to twelve Industrial Carbon Capture and Storage (ICCS) projects to conduct a Phase 1 feasibility study.^[105] The DOE plans to select 3 to 4 of those projects to proceed into Phase 2, design and construction, with operational startup to occur by 2015. Battelle Memorial Institute, Pacific Northwest Division, Boise, Inc., and Fluor Corporation are studying a CCS system for capture and storage of CO₂ emissions associated with the pulp and paper production industry. The site of the study is the Boise White Paper L.L.C. paper mill located near the township of Wallula in Southeastern Washington State. The plant generates approximately 1.2 MMT of CO₂ annually from a set of three recovery boilers that are mainly fired with black liquor, a recycled byproduct formed during the pulping of wood for paper-making. Fluor Corporation will design a customized version of their Econamine Plus carbon capture technology. The Fluor system also will be designed to remove residual quantities of remnant air pollutants from stack gases as part of the CO₂ capture process. Battelle is leading preparation of an Environmental Information Volume (EIV) for the entire project, including geologic storage of the captured CO₂ in deep flood basalt formations that exist in the greater region. The EIV will describe the necessary site characterization work, sequestration system infrastructure, and monitoring program to support permanent sequestration of the CO₂ captured at the plant.

In addition to individual carbon capture and sequestration projects, there are a number of U.S. programs designed to research, develop, and deploy CCS technologies on a broad scale. These include the National Energy Technology Laboratory's (NETL) Carbon Sequestration Program, regional carbon sequestration partnerships and the Carbon Sequestration Leadership Forum (CSLF).^[106][107]

SECARB

In October 2007, the Bureau of Economic Geology at the University of Texas at Austin received a 10-year, $38 million subcontract to conduct the first intensively monitored long-term project in the United States studying the feasibility of injecting a large volume of CO₂ for underground storage.^[108] The project is a research program of the Southeast Regional Carbon Sequestration Partnership (SECARB), funded by the National Energy Technology Laboratory of the U.S. Department of Energy (DOE).

The SECARB partnership will demonstrate CO₂ injection rate and storage capacity in the Tuscaloosa-Woodbine geologic system that stretches from Texas to Florida. The region has the potential to store more than 200 billion tons of CO₂ from major point sources in the region, equal to about 33 years of overall U.S. emissions at present rates. Beginning in fall 2007, the project will inject CO₂ at the rate of one million tons per year, for up to 1.5 years, into brine up to 10,000 feet (3,000 m) below the land surface near the Cranfield oil field, which lays about 15 miles (24 km) east of Natchez, Mississippi. Experimental equipment will measure the ability of the subsurface to accept and retain CO₂.

Kemper Project

Expected to be operational in 2016, Southern Company's and Mississippi Power's Kemper County energy facility (Kemper Project) will be the United States' first coal-fired plant to be built from the ground up with Carbon Capture and Storage.^[109] The Kemper Project will also include infrastructure for transporting byproducts like CO2 for Enhanced Oil Recovery (EOR), making the plant equipped as a CCS with EOR generation facility.^[110] With its advanced technologies, such as integrated gasification combined cycle, the Mississippi plant is expected to achieve very high efficiencies and capture 65% of its CO2 emissions.^[111]

Texas Clean Energy Project

The Texas Clean Energy Project (TCEP) is a “NowGen” Integrated Gasification Combined Cycle (IGCC) facility that will incorporate carbon capture, utilization and storage (CCUS) technology in a first-of-its-kind commercial clean coal power plant. This project is expected to be operational in 2018. It will be the first US-based power plant to combine both IGCC and capture 90% of its emissions.^[112]

Big Brown Steam Electric Station

Examples of carbon sequestration at an existing US coal plant can be found at utility company Luminant's pilot version at its Big Brown Steam Electric Station in Fairfield, Texas. This system is converting carbon from smokestacks into baking soda. Skyonic plans to circumvent storage problems of liquid CO₂ by storing baking soda in mines, landfills, to be sold as industrial or food grade baking soda,^[113] Green Fuel Technologies is piloting and implementing algae based carbon capture, circumventing storage issues by then converting algae into fuel or feed.^[114] though this may lead to re-release of the carbon.

United Kingdom

The government of the United Kingdom launched a first tender process for a CCS demonstration project in 2007. The project were to use post-combustion technology on coal-fired power generation at 300–400 megawatts or equivalent. The project aimed to be operational by 2014.^[115][116] The Government announced in June 2008 that four companies had pre-qualified for the competition: BP Alternative Energy International Limited, EON UK Plc, Peel Power Limited and Scottish Power Generation Limited.^[117] BP subsequently withdrew from the competition, claiming it could not find a power generator partner, and RWE npower sought a judicial review of the process after it did not qualify.^[118] This first CCS tender was cancelled in late 2011 when government could not reach agreement with the ScottishPower/Shell/National Grid consortium on terms and cost, for the project based on retrofitting the existing Longannet coal-fired power station in Scotland.

A second tender process was launched by government in 2012 as part of DECC's CCS Commercialisation Programme and two bidders, namely the Shell Peterhead gas-fired power station CCS project and the White Rose CCS project based upon a new oxy-fuel coal-fired unit at Drax power station were selected in 2013 to proceed to a funded front-end engineering and design phase. This second tender was cancelled in November 2015 following a government spending review at the time of the Chancellor's Autumn Statement.^[119]

Doosan Babcock has modified their Clean Combustion Test Facility (CCTF) in Renfrew, Scotland to create the largest Oxyfuel test facility currently in the world. Oxyfuel firing on pulverized coal with recycled flue gas demonstrates the operation of a full scale 40 MW burner for use in coal-fired boilers. Sponsors of the project include the UK Department for Business Enterprise and Regulatory Reform (BERR,) as well as a group of industrial sponsors and university partners comprising Scottish and Southern Energy (Prime Sponsor), E.ON UK PLC, Drax Power Limited, ScottishPower, EDF Energy, Dong Energy Generation, Air Products Plc (Sponsors), and Imperial College and University of Nottingham (University Partners).^[120]

In August 2010, clean energy new-comers B9 Coal announced their intention to join the competition with a CCS project in the North East of England. The proposal combines alkaline fuel cells with underground coal gasification for upwards of 90% carbon capture as a by-product. It is the only project of its kind to join the competition, using coal reserves in an environmentally friendly and efficient way.

In 2009 UK firm 2Co Energy was awarded planning permission for a £5bn power station and carbon-capture-and-storage project at Hatfield, near Doncaster and £164m of EU funding. Technology company Samsung agreed to take a 15% stake in the project.^[121] It is planned to construct a 60 km (37 mi) pipeline from Stainforth, near Hatfield in South Yorkshire to Barmston in the East Riding of Yorkshire. CO₂ would then be stored in natural porous rock beneath the North Sea. National Grid believes the project has the potential to reduce CO₂ emissions from power stations across Yorkshire and the Humber by up to 90% and both the proposed White Rose CCS project at Drax Power Station in North Yorkshire and the proposed Don Valley Power Project at Hatfield could benefit from the scheme.^{[122][123][124]}

In the Northeast of England, The Northeast of England Process Industry Cluster (NEPIC) of commodity chemical manufacturers are amongst the largest single point producers of carbon dioxide in the United Kingdom and they have created within NEPIC the Process Industry Carbon Capture and Storage Initiative^[125] (PICCSI) to study the possibility of a carbon capture and storage (CCS) solution being provided for the chemical and steel manufacturing industry on Teesside, as well as for any carbon based energy production. This CCS technology option is being considered as a result of climate change regulations and the carbon taxation that could become a prohibitive cost for such energy intensive industries.

The Crown Estate is responsible for storage rights on the UK continental shelf and it has facilitated work on offshore carbon dioxide storage technical and commercial issues.^[126]

China

In Beijing, as of 2009, one major power plant is capturing and re-selling a small fraction of its CO₂ emissions.^[127]

Germany

The German industrial area of Schwarze Pumpe, about 4 kilometres (2.5 mi) south of the city of Spremberg, is home to the world's first CCS coal plant.^[128] The mini pilot plant is run by an Alstom-built oxy-fuel boiler and is also equipped with a flue gas cleaning facility to remove fly ash and sulphur dioxide. The Swedish company Vattenfall AB invested some 70 million Euros in the two-year project, which began operation September 9, 2008. The power plant, which is rated at 30 megawatts, is a pilot project to serve as a prototype for future full-scale power plants.^[129][130] 240 tonnes a day of CO₂ are being trucked 350 kilometers (220 mi) where it will be injected into an empty gas field. Germany's BUND group called it a "fig leaf". For each tonne of coal burned, 3.6 tonnes of carbon dioxide is produced.^[131] The CCS program at Schwarze Pump ended in 2014 due to unvialbe costs and energy use.^[132]

German utility RWE operates a pilot-scale CO₂ scrubber at the lignite-fired Niederaußem power station built in cooperation with BASF (supplier of detergent) and Linde engineering.^[133]

In Jänschwalde, Germany,^[134] a plan is in the works for an Oxyfuel boiler, rated at 650 thermal MW (around 250 electric MW), which is about 20 times more than Vattenfall's 30 MW pilot plant under construction, and compares to today's largest Oxyfuel test rigs of 0.5 MW. Post-combustion capture technology will also be demonstrated at Jänschwalde.^[135]

Australia

The Federal Resources and Energy Minister Martin Ferguson opened the first geosequestration project in the southern hemisphere in April 2008. The demonstration plant is near Nirranda South in South Western Victoria. (35°19′S 149°08′E / 35.31°S 149.14°E) The plant is owned by the Cooperative Research Centre for Greenhouse Gas Technologies (CO2CRC). CO2CRC is a non profit research collaboration supported by government and industry. The project has stored and monitored over 65,000 tonnes of carbon dioxide-rich gas which was extracted from a natural gas reservoir via a well, compressed and piped 2.25 km to a new well. There the gas has been injected into a depleted natural gas reservoir approximately two kilometers below the surface.^[136][137] The project has moved to a second stage and is investigating carbon dioxide trapping in a saline aquifer 1500 meters below the surface. The Otway Project is a research and demonstration project, focused on comprehensive monitoring and verification.^[138]

This plant does not propose to capture CO₂ from coal-fired power generation, though two CO2CRC demonstration projects at a Victorian power station and research gasifier are demonstrating solvent, membrane, and adsorbent capture technologies from coal combustion.^[139] Currently, only small-scale projects are storing CO₂ stripped from the products of combustion of coal burnt for electricity generation at coal-fired power stations.^[140] Work currently being carried out by the GreenMag Group and the University of Newcastle and funded by the New South Wales and Australian Governments and industry intends to have a working mineral carbonation pilot plant in operation by 2013.^[41]

View the full list of Zero Emission Projects for fossil fuel power plant in Europe.^[141]

Limitations of CCS for power stations

Critics say large-scale CCS deployment is unproven and decades away from being commercialized. They say that it is risky and expensive and that a better option is renewable energy. Some environmental groups point out that CCS technology leaves behind dangerous waste material that has to be stored, just like nuclear power stations.^[142]

Another limitation of CCS is its energy penalty. The technology is expected to use between 10 and 40 percent of the energy produced by a power station.^[143] Wide-scale adoption of CCS may erase efficiency gains in coal power plants of the last 50 years, and increase resource consumption by one third. Even taking the fuel penalty into account, however, overall levels of CO₂ abatement would remain high at approximately 80–90%, compared to a plant without CCS.^[144] It is possible for CCS, when combined with biomass, to result in net negative emissions.^[145] Though, all of the currently (as of Feb 2011) operational BECCS (Bio-energy with carbon capture and storage) plants operate on point emissions other than power stations, such as biofuel refineries.^[146]

The use of CCS can reduce CO₂ emissions from the stacks of coal power plants by 85–90% or more, but it has no effect on CO₂ emissions due to the mining and transport of coal. It will actually "increase such emissions and of air pollutants per unit of net delivered power and will increase all ecological, land-use, air-pollution, and water-pollution impacts from coal mining, transport, and processing, because the CCS system requires 25% more energy, thus 25% more coal combustion, than does a system without CCS".^[147]

Another concern regards the permanence of storage schemes. Opponents to CCS claim that safe and permanent storage of CO₂ cannot be guaranteed and that even very low leakage rates could undermine any climate mitigation effect.^[143] In 1986 a large leakage of naturally sequestered CO₂ rose from Lake Nyos in Cameroon and asphyxiated 1,700 people. While the carbon had been sequestered naturally, some point to the event as evidence for the potentially catastrophic effects of sequestering carbon artificially.^[56][142]

On one hand, Greenpeace claims that CCS could lead to a doubling of coal plant costs.^[143] It is also claimed by opponents to CCS that money spent on CCS will divert investments away from other solutions to climate change. On the other hand, CCS is pointed out as economically attractive in comparison to other forms of low carbon electricity generation and seen by the IPCC and others as a critical component for meeting mitigation targets such as 450 ppm and 350 ppm.^{[148][149][150]}

Cost

Although the processes involved in CCS have been demonstrated in other industrial applications, no commercial scale projects which integrate these processes exist; the costs therefore are somewhat uncertain. Some recent credible estimates indicate that the cost of capturing and storing carbon dioxide is US$60 per ton,^[151] corresponding to an increase in electricity prices of about US 6c per kWh (based on typical coal-fired power plant emissions of 0.97 kg (2.13 lb) CO₂ per kWh). This would double the typical US industrial electricity price (now at around 6c per kWh) and increase the typical retail residential electricity price by about 50% (assuming 100% of power is from coal, which may not necessarily be the case, as this varies from state to state). Similar (approximate) price increases would likely be expected in coal dependent countries such as Australia, because the capture technology and chemistry, as well as the transport and injection costs from such power plants would not, in an overall sense, vary significantly from country to country.

The reasons that CCS is expected to cause such power price increases are several. Firstly, the increased energy requirements of capturing and compressing CO₂ significantly raises the operating costs of CCS-equipped power plants. In addition, there are added investment and capital costs. The process would increase the fuel requirement of a plant with CCS by about 25% for a coal-fired plant, and about 15% for a gas-fired plant.^[4] The cost of this extra fuel, as well as storage and other system costs, are estimated to increase the costs of energy from a power plant with CCS by 30–60%, depending on the specific circumstances. Pre-commercial CCS demonstration projects are likely to be more expensive than mature CCS technology; the total additional costs of an early large-scale CCS demonstration project are estimated to be €0.5-1.1 billion per project over the project lifetime. Other applications are possible. In the belief that use of sequestered carbon could be harnessed to offset the cost of capture and storage, Walker Architects published the first CO₂ gas CAES application, proposing the use of sequestered CO₂ for Energy Storage on October 24, 2008. To date the feasibility of such potential offsets to the cost have not been examined.^[152]

An estimate of costs of energy with and without CCS (2002 US$ per kWh)^[4]

	Natural gas combined cycle	Pulverized coal	Integrated gasification combined cycle
Without capture (reference plant)	0.03–0.05	0.04–0.05	0.04–0.06
With capture and geological storage	0.04–0.08	0.06–0.10	0.06–0.09
(Cost of capture and geological storage)	0.01–0.03	0.02–0.05	0.02–0.03
With capture and Enhanced oil recovery	0.04–0.07	0.05–0.08	0.04–0.08
All costs refer to costs for energy from newly built, large-scale plants. Natural gas combined cycle costs are based on natural gas prices of US$2.80–4.40 per GJ (LHV based). Energy costs for PC and IGCC are based on bituminous coal costs of US$1.00–1.50 per GJ LHV. Note that the costs are very dependent on fuel prices (which change continuously), in addition to other factors such as capital costs. Also note that for EOR, the savings are greater for higher oil prices. Current gas and oil prices are substantially higher than the figures used here. All figures in the table are from Table 8.3a in [IPCC, 2005].[4]

The cost of CCS depends on the cost of capture and storage, which varies according to the method used. Geological storage in saline formations or depleted oil or gas fields typically cost US$0.50–8.00 per tonne of CO₂ injected, plus an additional US$0.10–0.30 for monitoring costs. When storage is combined with enhanced oil recovery to extract extra oil from an oil field, however, the storage could yield net benefits of US$10–16 per tonne of CO₂ injected (based on 2003 oil prices). This would likely negate some of the effect of the carbon capture when the oil was burnt as fuel. Even taking this into account, as the table above shows, the benefits do not outweigh the extra costs of capture.

Cost of electricity generated by different sources including those incorporating CCS technologies can be found in cost of electricity by source. If CO₂ capture was part of a fuel cycle then the CO₂ would have value rather than be a cost. The proposed Solar Fuel or methane cycle proposed by the Fraunhofer Society amongst others is an example. This "solar fuel"^[153] cycle uses the excess electrical renewable energy to create hydrogen via electrolysis of water.^[154][155] The hydrogen is then combined with CO₂ to create synthetic natural gas SNG and stored in the gas network. See the latest Cost Report on the Cost of CO₂ Capture produced by the Zero Emissions Platform

Governments around the world have provided a range of different types of funding support to CCS demonstration projects, including tax credits, allocations and grants. The funding is associated with both a desire to accelerate innovation activities for CCS as a low-carbon technology and the need for economic stimulus activities. As of 2011, approximately US$23.5bn has been made available to support large-scale CCS demonstration projects around the world.^[156]

Carbon capture and storage and the Kyoto Protocol

One way to finance future CCS projects could be through the Clean Development Mechanism of the Kyoto Protocol. At COP16 in 2010, The Subsidiary Body for Scientific and Technological Advice, at its thirty-third session, issued a draft document recommending the inclusion of Carbon dioxide capture and storage in geological formations in Clean Development Mechanism project activities.^[157] At COP17 in Durban, a final agreement was reached enabling CCS projects to receive support through the Clean Development Mechanism.^[158]

Environmental effects

The theoretical merit of CCS systems is the reduction of CO₂ emissions by up to 90%, depending on plant type. Generally, environmental effects from use of CCS arise during power production, CO₂ capture, transport, and storage. Issues relating to storage are discussed in those sections.

Additional energy is required for CO₂ capture, and this means that substantially more fuel has to be used to produce the same amount of power, depending on the plant type. For new super-critical pulverized coal (PC) plants using current technology, the extra energy requirements range from 24 to 40%, while for natural gas combined cycle (NGCC) plants the range is 11–22% and for coal-based gasification combined cycle (IGCC) systems it is 14–25% [IPCC, 2005].^[159] Obviously, fuel use and environmental problems arising from mining and extraction of coal or gas increase accordingly. Plants equipped with flue-gas desulfurization (FGD) systems for sulfur dioxide control require proportionally greater amounts of limestone, and systems equipped with selective catalytic reduction systems for nitrogen oxides produced during combustion require proportionally greater amounts of ammonia.

IPCC has provided estimates of air emissions from various CCS plant designs (see table below). While CO₂ is drastically reduced though never completely captured, emissions of air pollutants increase significantly, generally due to the energy penalty of capture. Hence, the use of CCS entails a reduction in air quality. Type and amount of air pollutants still depends on technology. CO₂ is captured with alkaline solvents catching the acidic CO₂ at low temperatures in the absorber and releasing CO₂ at higher temperatures in a desorber. Chilled Ammonia CCS Plants have inevitable ammonia emissions to air. "Functionalized Ammonia" emit less ammonia, but amines may form secondary amines and these will emit volatile nitrosamines^[160] by a side reaction with nitrogendioxide, which is present in any flue gas even after DeNOx. Nevertheless, there are advanced amines in testing with little to no vapor pressure to avoid these amine- and consecutive nitrosamine emissions. Nevertheless, all the capture plants amines have in common, that practically 100% of remaining sulfur dioxide from the plant is washed out of the flue gas, the same applies to dust/ash.

Emissions to air from plants with CCS (kg/(MW•h))

	Natural gas combined cycle	Pulverized coal	Integrated gasification combined cycle
CO2	43 (-89%)	107 (−87%)	97 (−88%)
NOX	0.11 (+22%)	0.77 (+31%)	0.1 (+11%)
SOX	-	0.001 (−99.7%)	0.33 (+17.9%)
Ammonia	0.002 (before: 0)	0.23 (+2200%)	-
Based on Table 3.5 in [IPCC, 2005]. Between brackets the increase or decrease compared to a similar plant without CCS.

See also

• Bio-energy with carbon capture and storage
• Biosequestration
• Carbon capture and storage (timeline)
• Carbon cycle re-balancing
• Carbon sequestration
• Carbon sink
• Clean coal
• Comparisons of life-cycle greenhouse-gas emissions
• Eddy covariance
• Exhaust gas
• Flue-gas desulfurization
• Flue-gas emissions from fossil-fuel combustion
• Flue-gas stack
• Integrated Gasification Combined Cycle
• Landfill gas
• Limnic eruption
• Low-carbon economy
• Northeast of England Process Industry Cluster
• Solid sorbents for carbon capture

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Bibliography

• Environmental Challenges and Greenhouse Gas Control for Fossil Fuel Utilization in the 21st Century. Edited by M. Mercedes Maroto-Valer et al., Kluwer Academic/Plenum Publishers, New York, 2002: "Sequestration of Carbon Dioxide by Ocean Fertilization", p. 122. By M. Markels, Jr. and R.T. Barber.
• Nobel Intent: Carbon Dioxide Lakes in the Deep Ocean, September 19, 2006 @ 11:08 am - posted by John Timmer
• Solomon, Semere. (July 2006). Carbon Dioxide Storage: Geological Security and Environmental Issues Case Study on the Sleipner Gas Field in Norway. The Bellona Foundation. Retrieved November 7, 2006
• ICO2N - The Vision
• Stephens, Jennie C. (2006). "Growing interest in carbon capture and storage (CCS) for climate change mitigation. Sustainability". Science, Practice, & Policy 2 (2): 4–13.
• The illusion of clean coal - Climate change, Mar 5th 2009, The Economist print edition
• The Economist (2009) Trouble in store - Carbon capture and storage, Mar 5th 2009, The Economist print edition
• Bullis, K. (2009, October). Capturing carbon dioxide through cement production. Technology Review, 112(5)
• Biello, D. (2008, August 7). Cement from CO₂: a concrete cure for global warming?. Scientific American

Further reading

• Hester, Ronald E; Roy M. Harrison (2009). Carbon capture: sequestration and storage (Issues in environmental science and technology, 29. ed.). Royal Society of Chemistry. ISBN 978-1-84755-917-3
• Shackley, Simon; Clair Gough (2006). Carbon capture and its storage: an integrated assessment. Ashgate. ISBN 0754644995
• Wilson, Elizabeth J; David Gerard (2007). Carbon capture and sequestration : integrating technology, monitoring and regulation. Blackwell Publishing. ISBN 978-0-8138-0207-7
• Metz, Bert (2005). IPCC special report on carbon dioxide capture and storage. Intergovernmental Panel on Climate Change. Working Group III (Cambridge University Press). ISBN 0-521-86643-X

• Wilcox, Jennifer (2012). Carbon Capture. Springer. ISBN 978-1-4614-2214-3
• Smit, Berend; Jeffrey A Reimer; Curtis M Oldenburg; Ian C Bourg (2014). Introduction to Carbon Capture and Sequestration., Imperial College Press, ISBN 978-1-78326-327-1
• GA Mansoori, N Enayati, LB Agyarko (2016), Energy: Sources, Utilization, Legislation, Sustainability, Illinois as Model State, World Sci. Pub. Co., ISBN 978-981-4704-00-7

External links

• DOE Fossil Energy Department of Energy programs in carbon dioxide capture and storage.
• Algae based CCS, CO₂ Capture with Algae
• 2007 NETL Carbon Sequestration Atlas
• Scientific Facts on CO₂ Capture and Storage, a peer-reviewed summary of the IPCC Special Report on CCS.
• Carbon Capture: A Technology Assessment Congressional Research Service
• Carbon Sequestration News Recent news articles on CO₂ capture and storage.
• "Burying Climate Change: Efforts Begin to Sequester Carbon Dioxide from Power Plants", West Virginia hosts the world's first power plant to inject some of its CO₂ emissions underground for permanent storage, Scientific American, September 22, 2009.
• Mitigate your Carbon emissions by planting trees Green EU Initiative
• National Assessment of Geologic Carbon Dioxide Storage Resources: Results United States Geological Survey
• A Guide To Carbon Capture And Storage: Can carbon capture and storage save the climate from the consequences of fossil fuel burning?
• Powerplantccs Power Plant Carbon Capture, Storage, CO₂ Sequestration
• Paving the Legal Path for Carbon Sequestration from Coal 2009 journal article on CCS legal questions.
• MIT Carbon Capture and Sequestration