TABLE 3.
Example cumene inventory with in corporation of mock CBI
Flow name | Units | Source | Process attribution—Public |
Process attribution—CBI example |
|||||||
---|---|---|---|---|---|---|---|---|---|---|---|
Average U.S. LCI |
Facility count |
Maximum | Flow reliability score |
Average U.S. LCI |
Facility count |
Maximum | Flow reliability score |
% Change with CBI |
|||
Products and services: | |||||||||||
Cumene | kg | CDR | 1.00 | 8.00 | 1.00 | NA | 1.00 | 8.00 | 1.00 | ||
Heat inputs to production: | |||||||||||
Industrial processes; petroleum industry; process heaters; natural gas fired | MJ | e-GGRT | 0.14 | 3.00 | 4.09 | 2.00 | 0.11 | 3.00 | 4.09 | 2.00 | −22 |
External combustion boilers; industrial; natural gas; 10–100 million BTU/hr | MJ | e-GGRT | 0.098 | 2.00 | 4.83 | 2.00 | 0.28 | 3.00 | 4.83 | 2.00 | 184 |
External combustion boilers; industrial; process gas; petroleum refinery gas | MJ | e-GGRT | 0.20 | 4.00 | 2.84 | 2.00 | 0.63 | 5.00 | 2.62 | 2.00 | 212 |
Industrial processes; petroleum industry; process heaters; process gas fired | MJ | e-GGRT | 1.05 | 3.00 | 4.26 | 2.00 | 0.76 | 4.00 | 3.73 | 2.00 | −28 |
External combustion boilers; industrial; natural gas; >100 million BTU/hr | MJ | e-GGRT | 0.54 | 6.00 | 1.94 | 2.00 | 0.44 | 6.00 | 1.94 | 2.00 | −19 |
Releases: | |||||||||||
1,2,4-Trimethylbenzene | kg | TRI | 5.4E-08 | 5.00 | 7.0E-07 | 2.15 | 2.8E-07 | 6.00 | 1.3E-06 | 1.88 | 411 |
1,3-Butadiene | kg | NEI | 1.0E-07 | 5.00 | 4.1E-07 | 1.62 | 7.6E-08 | 6.00 | 3.6E-07 | 1.69 | −26 |
2,2,4-Trimethylpentane | kg | NEI | 6.4E-08 | 4.00 | 1.5E-07 | 2.00 | 5.0E-08 | 5.00 | 1.5E-07 | 2.00 | −23 |
Acetophenone | kg | NEI | 1.2E-06 | 3.00 | 0.0026 | 2.25 | 6.0E-07 | 3.00 | 3.6E-05 | 2.25 | −50 |
Ammonia | kg | TRI NEI | 3.4E-07 | 6.00 | 0.0017 | 2.33 | 5.4E-08 | 7.00 | 2.4E-05 | 2.96 | −84 |
Benzene | kg | NEI | 5.9E-06 | 8.00 | 6.0E-04 | 2.19 | 1.0E-05 | 9.00 | 2.3E-05 | 2.18 | 72 |
Benzo[g,h,i,]perylene | kg | TRI NEI | 8.1E-13 | 4.00 | 4.4E-12 | 3.39 | 1.3E-11 | 5.00 | 6.5E-11 | 3.77 | 1451 |
Carbon dioxide | kg | e-GGRT | 0.013 | 5.00 | 0.052 | 2.10 | 0.0096 | 6.00 | 0.046 | 2.03 | −26 |
Carbon monoxide | kg | NEI | 6.2E-07 | 7.00 | 2.6E-04 | 1.83 | 1.8E-06 | 8.00 | 4.7E-06 | 2.03 | 185 |
Chlorine | kg | NEI TRI | 1.5E-10 | 3.00 | 7.4E-09 | 4.52 | 5.4E-10 | 4.00 | 7.4E-09 | 3.89 | 271 |
Cumene | kg | NEI TRI | 1.9E-05 | 7.00 | 1.3E-04 | 2.21 | 1.9E-05 | 8.00 | 1.3E-04 | 2.19 | −1 |
Cumene hydroperoxide | kg | TRI | 3.0E-08 | 3.00 | 5.3E-06 | 1.31 | 1.8E-08 | 3.00 | 5.3E-06 | 1.31 | −40 |
Cyclohexane | kg | TRI | 7.0E-08 | 6.00 | 2.3E-07 | 1.99 | 6.5E-08 | 7.00 | 2.2E-07 | 1.80 | −6 |
Diethanolamine | kg | TRI NEI | 3.8E-08 | 3.00 | 9.5E-08 | 2.00 | 1.1E-07 | 4.00 | 4.5E-07 | 2.00 | 189 |
Dinitrogen monoxide | kg | e-GGRT | 4.5E-08 | 5.00 | 1.8E-07 | 1.99 | 3.6E-08 | 6.00 | 1.5E-07 | 1.94 | −21 |
Dioxin and dioxin compounds | kg | TRI | 4.2E-15 | 3.00 | 1.1E-12 | 2.98 | 2.5E-14 | 4.00 | 1.1E-12 | 2.59 | 488 |
Ethyl benzene | kg | NEI | 1.0E-07 | 7.00 | 1.3E-04 | 1.95 | 1.8E-07 | 8.00 | 6.6E-07 | 1.99 | 74 |
Ethylene | kg | TRI | 1.8E-06 | 5.00 | 7.5E-06 | 2.12 | 1.4E-06 | 6.00 | 6.6E-06 | 1.86 | −26 |
Ethylene glycol | kg | NEI TRI | 1.2E-09 | 2.00 | 5.0E-09 | 3.14 | 8.7E-10 | 3.00 | 4.4E-09 | 3.81 | −28 |
Formaldehyde | kg | NEI | 1.6E-09 | 2.00 | 9.1E-09 | 2.00 | 1.9E-09 | 3.00 | 9.1E-09 | 2.00 | 13 |
Hexane | kg | NEI | 1.8E-07 | 6.00 | 4.8E-07 | 2.01 | 1.9E-07 | 7.00 | 4.2E-07 | 2.03 | 5 |
Hydrochloric acid | kg | NEI TRI | 1.5E-08 | 4.00 | 5.3E-06 | 3.74 | 1.1E-08 | 5.00 | 5.3E-06 | 2.98 | −23 |
Hydrogen fluoride | kg | NEI | 4.7E-12 | 3.00 | 3.2E-11 | 4.08 | 9.2E-10 | 4.00 | 5.0E-09 | 3.43 | 19631 |
Lead | kg | TRI NEI | 2.9E-11 | 4.00 | 1.2E-09 | 4.32 | 3.2E-11 | 5.00 | 1.1E-09 | 4.53 | 8 |
Mercury | kg | NEI TRI | 1.6E-10 | 5.00 | 6.7E-10 | 2.30 | 1.3E-10 | 6.00 | 6.5E-10 | 2.94 | −20 |
Methane | kg | e-GGRT | 1.0E-05 | 5.00 | 5.0E-05 | 2.15 | 1.0E-05 | 6.00 | 4.5E-05 | 2.08 | 3 |
Methanol | kg | NEI TRI | 1.5E-07 | 5.00 | 1.2E-06 | 2.51 | 1.1E-07 | 5.00 | 1.2E-06 | 2.51 | −28 |
Methyl tert-butyl ether | kg | NEI | 4.7E-09 | 3.00 | 1.9E-08 | 2.00 | 5.6E-09 | 3.00 | 1.7E-08 | 2.00 | 20 |
Molybdenum trioxide | kg | TRI | 5.7E-11 | 2.00 | 5.2E-10 | 5.00 | 4.6E-11 | 3.00 | 5.2E-10 | 5.00 | −19 |
Naphthalene | kg | NEI | 1.2E-08 | 5.00 | 3.4E-08 | 2.00 | 3.3E-08 | 6.00 | 1.3E-07 | 2.02 | 181 |
Nickel | kg | NEI | 2.5E-10 | 3.00 | 1.7E-09 | 4.08 | 3.6E-10 | 4.00 | 1.7E-09 | 4.37 | 43 |
Nitrogen oxides | kg | NEI | 1.0E-06 | 7.00 | 3.2E-04 | 1.91 | 1.5E-06 | 8.00 | 2.2E-05 | 1.87 | 48 |
Phenol | kg | NEI TRI | 4.8E-07 | 5.00 | 1.0E-05 | 2.66 | 4.0E-07 | 6.00 | 9.8E-04 | 2.56 | −16 |
PM10 primary | kg | NEI | 1.8E-06 | 8.00 | 6.4E-05 | 2.79 | 4.0E-06 | 8.00 | 1.0E-04 | 3.03 | 128 |
Polycyclic aromatic compounds | kg | TRI NEI | 1.7E-09 | 5.00 | 7.0E-09 | 3.21 | 1.4E-09 | 6.00 | 6.9E-09 | 2.84 | −19 |
Propylene | kg | TRI | 7.8E-06 | 7.00 | 2.2E-05 | 2.10 | 6.4E-06 | 8.00 | 2.2E-05 | 1.90 | −19 |
Styrene | kg | NEI | 3.7E-09 | 3.00 | 1.5E-08 | 2.00 | 7.0E-09 | 4.00 | 2.3E-08 | 2.00 | 86 |
Sulfur dioxide | kg | NEI | 6.1E-07 | 7.00 | 2.5E-06 | 2.25 | 3.2E-06 | 7.00 | 1.4E-05 | 2.66 | 423 |
Sulfuric acid | kg | TRI | 2.0E-07 | 2.00 | 1.3E-06 | 1.33 | 5.5E-07 | 3.00 | 2.1E-06 | 1.58 | 179 |
Toluene | kg | TRI NEI | 1.3E-06 | 7.00 | 5.2E-06 | 2.00 | 1.4E-06 | 8.00 | 5.0E-06 | 2.03 | 5 |
Volatile organic compounds | kg | NEI | 6.2E-05 | 8.00 | 0.055 | 2.14 | 6.4E-05 | 8.00 | 3.5E-04 | 2.15 | 4 |
Xylenes (mixed isomers) | kg | NEI | 2.6E-07 | 7.00 | 9.3E-07 | 2.00 | 1.8E-06 | 7.00 | 8.6E-06 | 2.02 | 580 |
Notes: Results shown for heat inputs and air releases that occur at more than two facilities. Results include the process attribution refinement. Demonstration of the CBI inclusion approach uses a mock value of 158 thousand metric tons per year for any CBI chemical production instance.
CBI, confidential business information; CDR, Chemical Data Reporting; e-GGRT, Electronic GreenhouseGas Reporting Tool; NEI, National Emissions Inventory; LCI, life cycle inventory; TRI, toxics release inventory.