Carbon Capture and Utilization in the Industrial Sector

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Carbon Capture and Utilization in the Industrial Sector Pete Psarras, Stephen Comello, Praveen Bains, Panunya Charoensawadpong, Stefan Reichelstein, and Jennifer Wilcox Environ. Sci. Technol., Just Accepted Manuscript • DOI: 10.1021/acs.est.7b01723 • Publication Date (Web): 31 Aug 2017 Downloaded from http://pubs.acs.org on September 3, 2017

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Environmental Science & Technology

Carbon Capture and Utilization in the Industrial Sector

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Peter C. Psarras,1 Stephen Comello,2 Praveen Bains3, Panunya Charoensawadpong3, Stefan Reichelstein2, and Jennifer Wilcox1*

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1

Department of Chemical and Biological Engineering, Colorado School of Mines.

2

Graduate School of Business, Stanford University.

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Department of Energy Resources Engineering, Stanford University.

*Correspondence to: [email protected]

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Abstract: The fabrication and manufacturing of industrial commodities such as iron, glass and

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cement is carbon-intensive. A major reason capture of carbon dioxide from flue gases of

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industrial processes has not been widely adopted as a climate mitigation strategy is due to the

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lack of economic incentives for capturing CO2 on a scale that will impact climate. Yet,

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abatement opportunities do exist for the industrial sector, provided the scale of such processes is

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aligned well with CO2 utilization. This is important given that this sector accounts for 23% of

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total global emissions. This work develops a model that examines the full cost of separating,

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compressing and transporting CO2 of various industrial processes (sources), and pairing them

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with appropriate utilization opportunities (sinks). We find that – given the relatively higher

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concentrations of CO2 in flue gases from industrial processes – the full cost of abatement is

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lower than that of the power sector. Further, we find truck transportation is generally the low-

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cost alternative compared to pipeline transport for small volumes indicative of this kind of

ACS Paragon Plus Environment


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capture activity (100 kt CO2/a). We apply this methodology to a regional case study, which

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shows steel and cement manufacturing as having the lowest levelized cost of abatement.

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Introduction: The capture of CO2 from flue gases is viewed as one potential instrument to

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reduce global CO2 emissions. In terms of research, development and deployment, most of the

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existing work on carbon capture has focused on fossil-fuel based power generation (coal and

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natural gas). Yet abatement from industrial emissions has been largely overlooked, ignoring a

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substantial source of carbon dioxide. In 2013, the global industrial sector emitted approximately

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5.5 gigatonnes of carbon dioxide (Gt CO2), or 23% of total global CO2 emissions1 (see Figure S1

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for US breakdown)2. These emissions are the by-product of the production of commodities such

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as glass, cement, ammonia and steel – materials that form the essential fabric of the modern

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economy (2). To date, these commodities have few viable substitutes. Further, unlike the

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electricity sector, where mitigation can be achieved through a shift to cleaner, low-carbon energy

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sources such as wind or solar, there are no economic pathways that lead to zero CO2 emissions

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for most industrial commodity manufacturing. While overall production from such Essential

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Industrial Processes (EIPs) has declined in the US, it is projected to increase globally 45-60% by

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2050 to meet the demands of a rising global population and economic activity 3. We identify the

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following processes (products) as EIPs: aluminum, ammonia synthesis, mixed carbonate use,

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cement, biofuels (e.g., ethanol), ferroalloys, glass, iron and steel, lead, lime, magnesium,

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petrochemicals, phosphoric acid, pulp and paper, refining, silicon carbide manufacturing, soda

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ash production, titanium oxide, and zinc smelting (Figure 1).

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Industrial processes often yield exhaust streams containing higher CO2 content than the

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flue exhausts from fossil-fuel fired electricity production (e.g. coal and natural gas). It is


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generally accepted that there is an inverse relationship between cost of CO2 separation and initial

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dilution of a mixed feed stream

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may offer more economical abatement than what is projected in similar applications within the

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power sector.

4, 5

. As a consequence, carbon capture from industrial processes

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To assess the economic potential of carbon capture applied to EIPs, this study provides a

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cost analysis that aggregates the three major components of the carbon capture supply chain:

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separation, compression, and transport. We estimate the full economic cost, referred to as the

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levelized cost of CO2 separation (in dollars per tonne of CO2 captured). We then employ a geo-

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referencing approach, which links industrial sources to current and potential future CO2 sinks

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(utilization opportunities), to identify least cost pathways for abatement, given a local mix of

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supply and demand 6. The aim is to classify these EIPs based on carbon-capture economic

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viability for carbon capture, which is ultimately a combination of industry- and site-specific

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factors. Overall, our study identifies opportunities for CO2 emission reductions from industrial

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sources. The availability of low cost capture opportunities in a particular region may lead to an

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expanded CO2 commodity market, potentially displacing carbon dioxide production from natural

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reservoirs and/or specialty chemical manufacturing facilities. This replacement would have the

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effect of reducing overall CO2 emissions from an overall economy perspective7. Because prices

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from current CO2 sources such as natural reservoirs and select industrial facilities are low

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($7/tCO2 – $25/CO2)8 public policy in the form of carbon regulations and/or pricing may

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ultimately have to play a supportive role in enabling the kind of market we examine in this study.

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Methods

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Estimating the levelized Cost of CO2 Capture for Utilization: We calculate the full economic

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cost of carbon dioxide capture for utilization by using the general levelized product cost concept

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introduced in Ref.

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per tonne of CO2 of separating/capturing, compressing and transporting CO2. Our model does

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not include storage costs, because our end route is CO2 utilization, not geologic storage. This

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cradle-to-gate approach assigns all costs associated with utilization (e.g., further sweetening for

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use as a feedstock or injection in the case of EOR) to the sink operator. The LCO2 metric

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considers all fixed, variable and capacity related costs, in addition to discount rates and the effect

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of corporate income taxes, that must be incurred in order to deliver one tonne of purified CO2.

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The LCO2 concept is modular by construction and thus can be calculated for each element the

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carbon dioxide value chain (separation, compression and transport). The LCO2 is essentially a

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break-even metric, that is, the average price that would need to be received per tonne of CO2

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over the lifetime of a facility to achieve a net present value of zero on the initial investment in

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equipment and facilities. The three components of the levelized cost of CO2 capture and

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utilization are represented formally as:

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. Specifically, we refer to LCO2 as the levelized cost, measured in dollars

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= + + 87 88

where:

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•

LCS is the levelized cost of CO2 separation from flue gas [$/tCO2]

90

•

LCC is the levelized cost of CO2 compression [$/tCO2]


Eq. 1

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•

LCT is the levelized cost of CO2 transportation [$/tCO2]

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Generally, the cost of separation represents 60-80% of the total LCO2, with the cost of

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transportation being the most variable component based on the distance between source and sink.

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We now describe the calculation of each of these cost components.

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Levelized Cost of CO2 Separation: An inventory of the reactions for each EIP is provided in

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Table 1. These industrial processes can produce exhaust streams with higher CO2 content than

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power generation (typically 4-35% concentration), a factor that lends to a lower theoretical

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minimum work of separation

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(see Supplemental Information). Though the ratio of minimum

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work to real work (embodied in the second-law efficiency) scales non-linearly with dilution, CO2

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separation costs are generally found to be inversely related to the CO2 purity of the treated

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stream. This principle was first illustrated in the works of Thomas Sherwood, whereby the

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market price of various minerals were shown to scale inversely with concentration of that

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mineral11. Naturally, a single-parameter model is blind to several distinguishing process

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characteristics, such as separation technology or stream impurities. However, in a CO2 separation

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process, the balance of energy consumption (and thus cost) resides in the first steps of physical

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separation and – when applicable – regeneration of the separating agent. For these first-step

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dominant processes, energy and cost is shown to be most sensitive to target dilution, hence the

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effectiveness of the single-parameter Sherwood approach, and its continued use in cost

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modeling.4, 12-14 We expand upon this principle to build a cost model based on current capture

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costs and conditions. Given cost estimates for CO2 capture technologies from power generation,

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we use the Integrated Environmental Control Module (IECM)

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Specifically, the IECM provides estimates for the facility and operating costs (including fuel


15

to calibrate the model.


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costs) of electricity generation and carbon dioxide capture equipment for natural gas combined

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cycle (NGCC), sub-critical pulverized coal (PC) and integrated gasification combined cycle

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(IGCC) systems of various capacities (net power outputs), capture efficiencies and flow rates.

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Based on the methodology described and data provided in the Supplementary Information, these

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model output costs are used to determine the levelized cost of separation, LCS, for each

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combination of generation technology, peak capacity, capture efficiency and flow rate. In this

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study, 24 estimates of LCS (and LCC, discussed in the following page) were generated, based on

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the 3 generation technologies (NGCC, PC, IGCC), 2 capacities each (large and small) and 4

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capture rate (90%, 80%, 70%, 60%). These estimates became the basis for a cost equation using

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a multivariate regression, with LCS as the independent variable and capture rate (%), flue CO2

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concentration (%) and flow rate (tonnes/day) as the dependent variables (see also Supplementary

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Information). The resulting linear estimation yields:

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= 80.94 − 0.25 − 80.63 − 0.0006

Eq. 2

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This relationship is applied to each EIP to estimate LCS, assuming a 90% capture rate. These

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results, together with typical EIP conditions, are summarized in Table 2 and span a range of $0

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per tCO2 (for pure stream capture) to $70 per tCO2. While the cost of separation shows a clear

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inverse relationship with concentration, flow rate plays a smaller role as industrial flow rates are

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comparable in scale and cost of separation is less sensitive to variations in flow rate as CO2

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concentration increases (Figure 2). Note that literature costs of capture may deviate from

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calculated estimates based on differing assumptions regarding cost of capacity, operational costs

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(including fuel and electricity) and operational conditions. Analysis of model sensitivity to


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several factors has been conducted and is presented in SI. Moreover, Sherwood estimates align

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with processes with relatively low energy penalty and should be considered a lower bound in

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instances that deviate from this system design.

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calcium looping – shown to integrate well in cement facilities – against PCC MEA capture.17, 18

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As an example, compare oxyfiring with

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TABLE 1. Chemistry and scale of US essential industrial processes.a CO2 (Mt/a) Chemistry Process Combinedb 2.79 3.33 2Al O" + 3C → 4Al + 3CO 14.67 24.40 0.88CH& + 1.26air + 1.24H O → 0.88CO + N + 3H 0.48 1.48 Ca/MgCO" + heat → Ca/MgO + CO 65.79 68.22 CaCO" + heat → CaO + CO 40.80 40.80 C3 H4 O3 + yeast → 2C H7 OH + 2CO + heat 2.09 2.13 Fe O" + 2SiO + 7C → 2FeSi + 7CO Fe O" + 2MnO + 5C → 2FeMn + 5CO Fe O" + 2CrO + 5C → 2FeCr + 5CO Glass 1.18 5.34 various components + heat → CO + glass Iron and Steel 2C + O → 2CO 30.71 83.03 3CO + Fe O" → 2Fe + 3CO Lead 0.75 1.06 2PbO + C → 2Pb + CO 18.94 38.37 Lime CaCO" + heat → CaO + CO Magnesium 0.71 0.71 2MgO + C → 2Mg + CO 15.73 80.14 Petrochem. C H& + 3O → 2H O + 2CO H3PO4 1.72 2.72 CaCO" + H SO& + H O → CaSO& ∙ 2H O + CO 121.96 143.33 Pulp and Paper wood organics + O → CO ; CaCO" + heat → CaO + CO 69.34 188.05 Refining CH4."" OG.&" + 0.26O → 0.65CH4.4 + 0.27H O + 0.34CO SiC 0.12 0.12 SiO + 3C → SiC + 2CO Soda Ash 1.40 5.44 2Na CO" ∙ NaHCO" ∙ 2H O → 3Na CO" + 5H O + CO TiO2 1.44 2.47 2FeTiO" + 7Cl + 3C → 2TiCl& + 2FeCl" + 3CO Zinc 0.63 0.69 ZnO + CO → Zn + CO Total 391.25 691.84 a Source: EPA Greenhouse Gas Reporting Program, 2014 Commodity Aluminum Ammonia Carbonates Cement Ethanol Ferroalloys

b

Combined emissions = process + stationary combustion

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Levelized Cost of CO2 Compression: The IECM also provides estimates for the equipment and

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operating costs required to compress separated CO2. It is understood that the CO2 product is H2O

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saturated and compression costs include dehydration. To calculate the LCC as a function of

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capture efficiency and flow rate (similar to the calculation of LCS), the procedure for NGCC, PC

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and IGCC outlined above is repeated, however this time with compression equipment present.

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The capacity and operational costs calculated for separation are subtracted from the

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corresponding values that include both separation and compression costs. Using the total mass of

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CO2 separated for each calibrating case, we determine the LCC. Finally, in the same approach

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using a multivariate regression the resulting relationship to each EIP, the levelized cost of

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compression is determined. Results show a range between approximately $4 per tCO2 and $10

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per tCO2.

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TABLE 2. Minimum work and Sherwood-derived separation/capture cost estimations for various industries. Source Aluminum Ammonia Carbonates Cement Ethanol (biofuels) Ferroalloys Glass Iron and Steel

Lead Lime Magnesium Petrochemicals Pulp and Paper

CO2 Content (mol %)a

Ref.

Min. Work Estimated Cost (US$/tCO2 (kJ/mol CO2 Captured) b Captured)

4 – 10 6, 19, 20 8.2 – 10.8 30 – 99.9+ 22 0.0 – 5.0 20 24 6.2 14 – 33 25, 26 4.7 – 7.3

45.8 – 65.6 0.0f – 29.0 36.0 28.1 – 39.2

99.9+ 8 – 10 7 – 12 20 – 27

29 31-33 31, 34 25, 35

0.0 8.3 – 8.9 7.7 – 9.3 5.5 – 6.2

0.0f 46.3 – 50.6 44.4 – 54.9 31.4 – 34.2

15 20 15 30 – 99.9+ 8

38 31 31, 39 35, 40 41

7.1 6.2 7.1 0.0 – 5.0 8.9

40.5 34.4 40.7 0.0f – 28.6 48.0


Literature Estimates (2016 US$/t CO2 Captured) 68.2c,d – 76.3c,e 21.2c,g 57.3c,g, 68.4c,g, 54.8h – 95.3i, 12.7j

Ref. 21 23 23, 27, 28 30

21.7k – 24.4k, 23, 36, 37 32.6l – 44.0l, 57.3c,g

31.1m – 35.0m 61.7n

42-43

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Refining

3 – 20

44, 45

6.2 – 11.7

33.5 – 70.4

Silicon Carbide Soda Ash TiO2 Zinc Natural Gas Petroleum Coal

8 36 – 40 13 15 3–5 3–8 10 – 15

48 49 50 38 10, 40 10, 25 40, 52, 53

8.9 4.0 – 4.4 7.5 7.1 10.3 – 11.7 8.9 – 11.7 7.1– 8.3

51.4 25.6 – 26.7 41.2 40.2 57.2 – 69.9 47.0 – 69.0 36.5 – 42.7

a

44.8o, 57.0p 92.8q

45-47

76.3r

51

37.1 – 54.6s

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Range in composition due to different processes or different capture points within the same process. When not directly reported, values were

estimated from a complete mass balance assuming NG fuel and 15% excess air; b calculated assuming 99.5% purity and 90% capture, Ref. 10; c includes cost of compression; d calculated at 10% CO2 purity; e calculated at 4% CO2 purity; f for near pure streams, separation costs are considered in the compression and dehydration stage; g includes costs for transport and storage; h oxycombustion; i post-combustion MEA; j includes compression and dehydration; k selexol capture from the blast furnace; l post-combustion capture from blast furnace; m capture using precombustion shift technology; n amine capture from boiler; o PCC from gasifier exhaust; p SMR with CCS, cost avoided; q PCC on combined stack (9% CO2), cost avoided; r MEA PCC, 90% efficiency, cost avoided; s PCC from supercritical pulverized coal, includes compression.

158 159 160

Levelized Cost of CO2 Transportation: Generally, there are two methods of transport: pipeline

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and tanker delivery (trucking). Transport via rail could be viable if the source and sink were

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located proximal to railheads, though economics rarely prove favorable over short distances (
6250

Sink Demand (kt CO2 ) 500 250 0.0

Figure 1. National distribution of essential industrial processes. Graduated symbols denote potential CO2 capture volume (at 90% capture rate).



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Figure 2. Prediction of capture costs from power (black circles) of varying gas flow rates (low to high). This data is used to predict levelized costs of capture for several irreplaceable industries (colored circles and diamonds). Not shown are cost points for streams of 99.9+% CO2 purity, for which the cost of capture is assumed to approach zero.

CO2 Sinks Plastics/Polymers Manufacturing Fire Proo ng Refrigeration Industrial Gas Manufacturing Beverage Carbonation Enhanced Oil Recovery Soda Bicarbonate Manufacturing Urea Manufacturing Gum and Wood Chemicals

Sink Demand (kt CO2 per year) < 150 150.01 – 600 600.01 – 1200 >1200

Source Output (kt CO2 ) 15,000 5,000 0.0


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Figure 3. National distribution of CO2 utilization opportunities. Graduated symbols denote CO2 demand. Enhanced oil recovery dominates demand but is geographically isolated from industrial emitters in the Northeast and West coast, where smaller scale opportunities may play a more prominent role. 369

Figure 4. LCO2 and relative quantity delivered to sinks, PA case study. 370 371 372

References:

373

1.

374

Assessment Report of the Intergovernmental Panel on Climate Change; [Core Writing Team, R.K. Pachauri and

375

L.A. Meyer (eds.)]. IPCC, Geneva, Switzerland, , 2014; p 25.

376

2.

377

Emissions. Accessed January 16, 2016; 2015.

378

3.

379

http://www.ipcc.ch/ipccreports/sres/emission/index.php?idp=99 Accessed September 2, 2015; 2015.

IPCC Climate Change 2014: Synthesis Report. Contribution of Working Groups I, II and III to the Fifth

U.S. Environmental Protection Agency; (EPA) US GHG Inventory Chapter 2: Trends in Greenhouse Gas

Intergovermental Panel on Climate Change; (IPCC) Emissions Scenarios. Available at



380

4.

House, K. Z.; Baclig, A. C.; Ranjan, M.; van Nierop, E. A.; Wilcox, J.; Herzog, H. J., Economic and

381

energetic analysis of capturing CO2 from ambient air. Proceedings of the National Academy of Sciences 2011, 108,

382

(51), 20428-20433.

383

5.

Grübler, A., Technology and global change. Cambridge University Press: 2003.

384

6.

Solomon, S., Climate change 2007-the physical science basis: Working group I contribution to the fourth

385

assessment report of the IPCC. Cambridge University Press: 2007; Vol. 4.

386

7.

387

2014, 74, 579-588.

388

8.

Denbury Resources 2016 Annual Report; Plano, TX, 2016.

389

9.

Reichelstein, S.; Rohlfing-Bastian, A., Levelized Product Cost: Concept and Decision Relevance. The

390

Accounting Review 2014, 90, (4), 1653-1682.

391

10.

Wilcox, J., Carbon capture. Springer: New York, 2012.

392

11.

Sherwood, T. K., Mass Transfer Between Phases. Phi Lambda Upsilon, Penn State University, University

393

Park, PA: 1959.

394

12.

395

Technoeconomic Benchmarks in the Electroreduction of CO2. ChemSusChem 2016, 9, (15), 1972-1979.

396

13.

397

Design and Synthesis of Sustainable Integrated Biorefinery for Pharmaceutical Products from Palm-Based Biomass.

398

Process Integration and Optimization for Sustainability 2017, 1, (2), 135-151.

399

14.

400

Recycling. Environmental Science & Technology 2007, 41, (21), 7543-7550.

401

15.

402

storage. Energy policy 2007, 35, (9), 4444-4454.

403

16.

404

systematic review of carbon capture and storage (CCS) applied to the iron and steel, cement, oil refining and pulp

405

and paper industries, as well as other high purity sources. Int. J. Greenhouse Gas Control 2017, 61, 71-84.

406

17.

407

Systems and Policies 2012, (2012), 17.

Comello, S.; Reichelstein, S., Incentives for early adoption of carbon capture technology. Energy Policy

Verma, S.; Kim, B.; Jhong, H. R.; Ma, S.; Kenis, P. J. A., A Gross‐Margin Model for Defining

Ng, S. Y.; Ong, S. Y.; Ng, Y. Y.; Liew, A. H. B.; Ng, D. K. S.; Chemmangattuvalappil, N. G., Optimal

Dahmus, J. B.; Gutowski, T. G., What Gets Recycled: An Information Theory Based Model for Product

Rubin, E. S.; Chen, C.; Rao, A. B., Cost and performance of fossil fuel power plants with CO2 capture and

Leeson, D.; Mac Dowell, N.; Shah, N.; Petit, C.; Fennell, P. S., A Techno-economic analysis and

Fennell, P. S.; Florin, N.; Napp, T.; Hills, T., CCS from industrial sources. Sustainable Technologies,


Page 22 of 27

Page 23 of 27


408

18.

Dean, C.; Hills, T.; Florin, N.; Dugwell, D.; Fennell, P. S., Integrating calcium looping CO2 capture with

409

the manufacture of cement. Energy Procedia 2013, 37, 7078-7090.

410

19.

411

Aluminum Industries in the UAE: An Empirical Analysis. Energy Procedia 2013, 37, 7732-7740.

412

20.

413

http://www.phinix.net/services/Energy_Management/Improving_Energy_Efficiency.pdf. Accessed October 14,

414

2015. 2007.

415

21.

416

Capture from Aluminium Production. Energy Procedia 2014, 51, 184-190.

417

22.

418

(UK) Ltd.; 2010.

419

23.

420

Global CCS Institute. Canberra, Australia: Global CCS Institute 2011.

421

24.

422

Product Use. Accessed January 16, 2016; 2015.

423

25.

424

of isolated adsorbed atoms. Surf. Sci. 1973, 36, (1), 317-352.

425

26.

426

industry. Tannenstrasse: European Cement Research Academy 2007, 96.

427

27.

428

from a cement plant–technical possibilities and economical estimates, 2006, pp 19-22.

429

28.

430

Industry. Energy Procedia 2009, 1, (1), 87-94.

431

29.

432

45, (5), 28-29.

433

30.

Levina, E.; Bennett, S.; McCoy, S., Technology roadmap: carbon capture and storage. OECD/IEA: 2013.

434

31.

Intergovernmental Panel On Climate Change; (IPCC), 2006 IPCC guidelines for national greenhouse gas

435

inventories. 2006.

Tsai, I. T.; Al Ali, M.; El Waddi, S.; Zarzour, O. A., Carbon Capture Regulation for The Steel and

Das, S. K., Improving Energy Efficiency in Aluminum Melting. Available at

Mathisen, A.; Sørensen, H.; Eldrup, N.; Skagestad, R.; Melaaen, M.; Müller, G. I., Cost Optimised CO2

Zakkour, P., Cook, G. CCS Roadmap for Industry: High-Purity CO2 Sources. Carbon Counts Company

Parsons, W., Economic assessment of carbon capture and storage technologies: 2011 update. Report for the

U.S. Environmental Protection Agency; (EPA) US GHG Inventory Chapter 4: Industrial Processes and

Steele, W. A., The physical interaction of gases with crystalline solids: I. Gas-solid energies and properties

Hoenig, V.; Hoppe, H.; Emberger, B., Carbon capture technology-options and potentials for the cement

Hegerland, G.; Pande, J. O.; Haugen, H. A.; Eldrup, N.; Tokheim, L. A.; Hatlevik, L. M. In Capture of CO2

Barker, D. J.; Turner, S. A.; Napier-Moore, P. A.; Clark, M.; Davison, J. E., CO2 Capture in the Cement

Rushing, S. A., Merchant Carbon Dioxide Sourcing: The Ethanol Perspective. CryoGas International 2007,



436

32.

Holappa, L., Towards sustainability in ferroalloy production. South African Institute of Mining and

437

Metallurgy. Journal 2010, 110, (12), 703-710.

438

33.

439

International Ferroalloys Congress. 2013.

440

34.

441

steady-state computation fluid dynamics. Appl. Therm. Eng. 2013, 52, (2), 555-565.

442

35.

443

Change 1995, 29, (4), 439-461.

444

36.

Gielen, D., CO2 removal in the iron and steel industry. Energy Convers. Manage. 2003, 44, (7), 1027-1037.

445

37.

IEA CO2 capture and storage: a key carbon abatement option; Paris, France: International Energy Agency,

446

2008.

447

38.

448

(1), 30-40.

449

39.

450

Emissions from Chinese Magnesium Production. Environmental Science & Technology 2015, 49, (21), 12662-

451

12669.

452

40.

453

Technol. 2010, 101, (10), 3311-3319.

454

41.

455

https://www.iea.org/publications/freepublications/publication/tracking_emissions.pdf 2007.

456

42.

457

assessment. Mitigation and Adaptation Strategies for Global Change 2006, 11, (5-6), 1129-1150.

458

43.

459

Tobin, D.; Gilmartin, J. J.; Steffensen, E. J., Overcoming business model uncertainty in a carbon dioxide capture and

460

sequestration project: Case study at the Boise White Paper Mill. Int. J. Greenhouse Gas Control 2012, 9, 91-102.

461

44.

462

D., Application of Advanced Technologies for CO2 Capture From Industrial Sources. Energy Procedia 2013, 37,

463

7176-7185.

Ladam, Y.; Tangstad, M.; Ravary, B., Energy Mapping of Industrial Ferroalloy Plants. The thirteenth

Díaz-Ibarra, O.; Abad, P.; Molina, A., Design of a day tank glass furnace using a transient model and

Farla, J. C. M.; Hendriks, C. A.; Blok, K., Carbon dioxide recovery from industrial processes. Climatic

Wu, J. C. S., Photocatalytic reduction of greenhouse gas CO2 to fuel. Catalysis surveys from Asia 2009, 13,

Gao, F.; Liu, Y.; Nie, Z.-R.; Gong, X.; Wang, Z., Variation Trend and Driving Factors of Greenhouse Gas

Xu, Y.; Isom, L.; Hanna, M. A., Adding value to carbon dioxide from ethanol fermentations. Bioresour.

International Energy Agency; (IEA), Tracking Industrial Energy Efficiency and CO2 Emissions.

Möllersten, K.; Gao, L.; Yan, J., CO2 capture in pulp and paper mills: CO2 balances and preliminary cost

McGrail, B. P.; Freeman, C. J.; Brown, C. F.; Sullivan, E. C.; White, S. K.; Reddy, S.; Garber, R. D.;

Romano, M. C.; Anantharaman, R.; Arasto, A.; Ozcan, D. C.; Ahn, H.; Dijkstra, J. W.; Carbo, M.; Boavida,


Page 24 of 27

Page 25 of 27


464

45.

van Straelen, J.; Geuzebroek, F.; Goodchild, N.; Protopapas, G.; Mahony, L., CO2 capture for refineries, a

465

practical approach. Int. J. Greenhouse Gas Control 2010, 4, (2), 316-320.

466

46.

467

in Australia. Int. J. Greenhouse Gas Control 2011, 5, (1), 49-60.

468

47.

469

Greenhouse Gas Emissions at North American Refineries. Environmental Science & Technology 2017, 51, (3),

470

1918-1928.

471

48.

472

CO2 and water vapor to hydrocarbon fuels. Nano Lett. 2009, 9, (2), 731-737.

473

49.

474

carbon dioxide to hydrocarbons. Acs Nano 2010, 4, (3), 1259-1278.

475

50.

476

fluidized bed chlorination for preparation of TiCl 4. Transactions of Nonferrous Metals Society of China 2010, 20,

477

(1), 128-134.

478

51.

479

Plants. Environmental Science & Technology 2012, 46, (6), 3076-3084.

480

52.

481

Publishing House: 2007.

482

53.

483

opportunity for membranes. Journal of Membrane Science 2010, 359, (1), 126-139.

484

54.

485

Control 2015, 40, 378-400.

486

55.

Metz, B.; Davidson, O.; de Coninck, H.; Loos, M.; Meyer, L., Carbon dioxide capture and storage. 2005.

487

56.

Hasan, M. M. F.; Boukouvala, F.; First, E. L.; Floudas, C. A., Nationwide, regional, and statewide CO2

488

capture, utilization, and sequestration supply chain network optimization. Industrial & Engineering Chemistry

489

Research 2014, 53, (18), 7489-7506.

Ho, M. T.; Allinson, G. W.; Wiley, D. E., Comparison of MEA capture cost for low CO2 emissions sources

Motazedi, K.; Abella, J. P.; Bergerson, J. A., Techno–Economic Evaluation of Technologies to Mitigate

Varghese, O. K.; Paulose, M.; LaTempa, T. J.; Grimes, C. A., High-rate solar photocatalytic conversion of

Roy, S. C.; Varghese, O. K.; Paulose, M.; Grimes, C. A., Toward solar fuels: photocatalytic conversion of

Xiong, S.-F.; Yuan, Z.-F.; Cong, X. U.; Liang, X. I., Composition of off-gas produced by combined

Rubin, E. S.; Zhai, H., The Cost of Carbon Capture and Storage for Natural Gas Combined Cycle Power

Elanchezhian, C.; Saravanakumar, L.; Ramnath, B. V., Power Plant Engineering. I.K. International

Merkel, T. C.; Lin, H.; Wei, X.; Baker, R., Power plant post-combustion carbon dioxide capture: an

Rubin, E. S.; Davison, J. E.; Herzog, H. J., The cost of CO2 capture and storage. Int. J. Greenhouse Gas



490

57.

Knoope, M. M. J.; Guijt, W.; Ramírez, A.; Faaij, A. P. C., Improved cost models for optimizing CO2

491

pipeline configuration for point-to-point pipelines and simple networks. Int. J. Greenhouse Gas Control 2014, 22,

492

25-46.

493

58.

494

Consortium 2003.

495

59.

496

Available at http://www3.epa.gov/climatechange/ccs/. Accessed 11/1/2015; 2011.

497

60.

498

of carbon dioxide. Energy & Environmental Science 2010, 3, (1), 43-81.

499

61.

500

capture, utilization and storage (CCUS) to enhanced oil recovery. Center for Climate and Energy Solutions 2012.

501

62.

502

https://www.globalccsinstitute.com/sites/www.globalccsinstitute.com/files/publications/14026/accelerating-uptake-

503

ccs-industrial-use-captured-carbon-dioxide.pdf 2011.

504

63.

505

Journal of Supercritical Fluids 2004, 28, (2), 121-191.

506

64.

507

1998, 75, (12), 1641.

508

65.

509

2365-2387.

510

66.

511

Operations. In 2012.

512

67.

513

Flooding Conference. In (2013).

514

68.

515

Bituminous Coal (PC) and Natural Gas to Electricity Revision 3; 2015.

Berwick, M. D.; Farooq, M., Truck costing model for transportation managers. Mountain-Plains

United States Environmental Protection Agency; (EPA) Carbon Dioxide Capture and Sequestration,

Mikkelsen, M.; Jorgensen, M.; Krebs, F. C., The teraton challenge. A review of fixation and transformation

Melzer, L. S., Carbon dioxide enhanced oil recovery (CO2 EOR): Factors involved in adding carbon

Brinckerhoff, P., Accelerating the uptake of CCS: industrial use of captured carbon dioxide.

Beckman, E. J., Supercritical and near-critical CO2 in green chemical synthesis and processing. The

Wai, C. M.; Hunt, F.; Ji, M.; Chen, X., Chemical reactions in supercritical carbon dioxide. J. Chem. Educ.

Sakakura, T.; Choi, J.-C.; Yasuda, H., Transformation of Carbon Dioxide. Chem. Rev. 2007, 107, (6),

DiPietro, P.; Balash, P.; Wallace, M., A Note on Sources of CO2 Supply for Enhanced-Oil-Recovery

DiPietro, P., Murrell, G, North American CO2 Supply and Developments. presented at the 19th Annual CO2

Fout, T.; Gerdes, K.; Shultz, T. Cost and Performance Baseline for Fossil Energy Plants Volume 1a:

516


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