Refinery CO2 Management Strategies
Technology Solutions to Reduce Carbon Footprint and Meet Business Sustainability Goals
According to the US Dept. of Energy's Energy Information Administration (EIA), in 2006 global, energy-related emissions of CO2 totaled 29.195B mt, and petroleum refining was responsible for approximately 5% of this total. Refinery emissions can be almost entirely attributed to fuel combustion, which is in turn affected by the types of crudes processed and the product slates chosen.
More specifically, most of the emissions of CO2 from refineries are due to stationary combustion devices. These emissions are also referred to as energy-related emissions. At a hypothetical 250K-b/d refinery with a hydrogen plant and an FCCU, the CO2 emissions from various sources, as estimated by the American Petroleum Institute, are listed in the following table.
| Source (fuel used) | Number of units | CO2 emissions, MM mt/y |
| Combustion, stationary devices | 2.960 | |
| Steam boilers (refinery gas) | 10 | 1.160 |
| Process heaters (refinery gas) | 40 | 1.130 |
| FCCU CO boilers (refinery gas) | 1 | 0.079 |
| Internal combustion engines (natural gas) | 12 | 0.036 |
| Gas turbines (natural gas) | 3 | 0.378 |
| Flares | N.A. | 0.154 |
| Incinerators for SRU and tail gas treatment | 4 | 0.020 |
| Combustion, indirect | 0.033 | |
| Purchased electricity | — | 0.033 |
| Venting | 2.570 | |
| Hydrogen plant (natural gas) | N.A. | 0.367 |
| Hydrogen plant (refinery gas) | N.A. | 0.232 |
| FCCU regenerator (coke) | 1 | 1.970 |
| Crude tanks | N.A. | — |
| Maintenance and turnaround | N.A. | Included with flaring |
Refinery fuels include: coke; light hydrocarbon gases and liquid fuels, both of which are internally produced; and imported natural gas. It is clear that, per unit of energy, the refinery fuels differ significantly in the amounts of CO2 that are produced by their combustion, with natural gas having about one half the emissions of coke, as illustrated in the table below.
| Fuel | Refinery use | CO2 emissions factor | |
| MM mt/quad (MM mt/EJ) | Mass or volume basis | ||
| Natural gas |
|
53.15 (50.38) | 120.6 lb/1,000ft3 1.932 mt/1,000m3 |
| Refinery gas |
|
64.10 (60.80) | — |
| Distillate fuel oil |
|
73.19 (69.37) | 940.1 lb/b 2.682 mt/m3 |
| Residual fuel oil |
|
78.87 (74.76) | 1,093.4 lb/b 3.119 mt/m3 |
| Coke |
|
102.10 (96.78) | 1,356.5 lb/b 3.870 mt/m3 3.384 mt/mt |
| Coal |
N.A. | 93.20 (88.34) | 2.16 mt/mt |
As is known in the refining industry, crude quality plays a major role in determining refinery GHG emissions; lower API gravity and higher sulfur content correlate to increased refinery CO2 emissions. Not surprisingly, crudes with lower API gravity and higher sulfur content also correlate to greater energy intensity (energy per barrel of crude processed) and process intensity (combined capacity of vacuum distillation, coking, thermal cracking, FCC, and hydrocracking divided by the capacity of the atmospheric distillation unit). These correlations are thought to be attributed to two major factors. First, lighter, sweeter crudes require less conversion and desulfurization; and second, for lighter, sweeter crudes, the refinery's energy requirements are met by more low-carbon fuel gas and less coke, fuel oil, and other higher-carbon streams. On the other hand, many heavy, sour crudes will also contain high levels of nitrogen and metals, requiring further processing and adding to refinery CO2 emissions per barrel of crude processed. However, even crudes with similar API gravity, sulfur, nitrogen, and metals content will not necessarily yield similar amounts of CO2 per unit of product produced, because other crude properties such as the distribution of hydrocarbons (i.e., naphtha, distillates, gas oil), and the type of heteroatom compounds play a role in emissions, as well.
A refiner can perform a life-cycle assessment (LCA) or "well-to-wheels" analysis of the environmental impacts of different transportation fuels. In fact, the allocation of refinery CO2 emissions to individual petroleum products is extremely useful when a refinery wants to control its variable costs associated with CO2 emissions from different products. The complexity of today's refineries—in which a given product (e.g., gasoline) is involved with several refining units and a given refining unit produces multiple products—means that there is no unique way to allocate emissions to finished products. One approach that has been used is to perform the allocation in a way that reflects how the refinery's emissions would be changed by a quantitative variation in the product slate, as discussed in this Report. An example is shown in the following table.
| Refinery configuration* | CO2 emissions, mt CO2/mt product | ||||
| LPG | Naphtha + gasoline | Diesel | Fuel oil | Overall refinery, mt CO2/mt crude | |
| HSK | 0.297 | 0.287 | 0.138 | 0.185 | 0.205 |
| HSK + VB + FCC | 0.943 | 0.416 | 0.172 | 0.374 | 0.337 |
| HSK + VB + HCU | 0.362 | 0.500 | 0.174 | 0.290 | 0.325 |
| HSK + DC + HCU | 0.318 | 0.420 | 0.171 | 0.503 | 0.329 |
| HSK + VB + FCC + HCU | 0.478 | 0.414 | 0.204 | 0.445 | 0.362 |
| *HSK—hydroskimming, VB— visbreaking, DC— delayed coking, FCC— fluid catalytic cracking, HCU— hydrocracking | |||||
However, there are concerns with the allocations mentioned above. One is that they might not reflect what happens when marginal changes occur in the product slate. At present, schemes are being developed that use optimization routines.
This Report looks at how production of CO2 by refineries is being impacted by the fuels that are being used, the crudes that are being processed, and the product slate that is being produced. The allocations of emissions to specific refinery fuels and products are also covered. There are detailed discussions on the implementation of refinery carbon accounting; i.e., means for monitoring and estimating CO2 emissions. Furthermore, case studies are presented to examine the costs and benefits of various options and to identify competition in market supply and demand of combustion fuel, crude oils, and refined products on regional and global bases.
