| Literature DB >> 31909259 |
C X Low1, W Y Ng1, Z A Putra1, K B Aviso2, M A B Promentilla2, R R Tan2.
Abstract
Identification of appropriate clean technologies for industrial implementation requires systematic evaluation based on a set of criteria that normally reflect economic, technical, environmental and other aspects. Such multiple attribute decision-making (MADM) problems involve rating a finite set of alternatives with respect to multiple potentially conflicting criteria. Conventional MADM approaches often involve explicit trade-offs in between criteria based on the expert's or decision maker's priorities. In practice, many experts arrive at decisions based on their tacit knowledge. This paper presents a new induction approach, wherein the implicit preference rules that estimate the expert's thinking pathways can be induced. P-graph framework is applied to the induction approach as it adds the advantage of being able to determine both optimal and near-optimal solutions that best approximate the decision structure of an expert. The method elicits the knowledge of experts from their ranking of a small set of sample alternatives. Then, the information is processed to induce implicit rules which are subsequently used to rank new alternatives. Hence, the expert's preferences are approximated by the new rankings. The proposed induction approach is demonstrated in the case study on the ranking of Negative Emission Technologies (NETs) viability for industry implementation.Entities:
Keywords: Chemical engineering; Clean technologies; Decision analysis; Induction; Optimal selection; P-Graph; Simple additive weighting
Year: 2019 PMID: 31909259 PMCID: PMC6940623 DOI: 10.1016/j.heliyon.2019.e03083
Source DB: PubMed Journal: Heliyon ISSN: 2405-8440
Figure 1The flow of proposed induction network.
Figure 2(a) Hierarchical decision structure for 2 criteria and 2 alternatives and (b) P-graph representation translated from Delta Matrix which illustrates the decision structure in part (a).
Descriptions of NET alternatives in Set I (adapted from [23] to [26]).
| Category | NET alternatives | Descriptions |
|---|---|---|
| Mineralization | Biochar | Sequestration of thermochemically stabilized biomass carbon in soil. |
| Enhanced weathering | Acceleration of mineral carbonation process in soil. | |
| Pressurized | Bioenergy and Carbon Capture Storage (BECCS) | Combination of biomass and Carbon Capture and Storage (CCS) technology. |
| Direct Air Capture (Artificial Tree) | Adsorption and sequestration of CO2 using amine-based sorbent and CCS technology. | |
| Direct Air Capture (Lime-soda Process) | Adsorption and sequestration of CO2 using sodium hydroxide in scrubbing tower and CCS. | |
| Oceanic | Ocean Liming (Calcination) | Addition of lime into ocean for carbonation process. |
| Ocean Liming (Electrochemical Splitting) | Sequestration of Ca(HCO3)2 aq. produced from the electrolysis process into the ocean. |
Descriptions of the criteria involved in the decision-making problem.
| Criteria | Descriptions |
|---|---|
| Technology Status (C1) | To approximate the technology status of NETs by considering a technology's scalability and maturity for industry deployment [ |
| Potential Capture Capacity (C2) | To estimate the capability of the NETs to remove anthropogenic CO2. |
| Cost (C3) | To estimate the financial feasibility of the NETs by considering the costs of material inputs, equipment, utility and implementation. |
| Energy Requirement (C4) | To approximate the energy feasibility of the NETs. |
Extended Decision Matrix of 7 alternatives with respect to the 4 criteria (adapted from [23] to [26]).
| NET alternatives | Criteria | |||
|---|---|---|---|---|
| Technical status (TRL) | Potential Capacity | Cost | Energy Requirement | |
| Biochar | 1.00 | 0.11 | 0.65 | 1.00 |
| BECCS (Combustion) | 1.00 | 0.58 | 0.63 | 0.42 |
| DAC (Artificial Tree) | 0.67 | 1.00 | 0.60 | 0.42 |
| DAC (lime-soda process) | 1.00 | 1.00 | 0.00 | 0.00 |
| Ocean Liming (Calcination) | 0.67 | 0.00 | 0.92 | 0.24 |
| Ocean Liming (Electrochemical splitting) | 0.33 | 0.00 | 0.69 | 0.19 |
| Enhanced weathering | 0.00 | 0.00 | 1.00 | 0.16 |
Figure 3Maximal structure of training set.
Figure 4Optimal Network structure.
Performance of NET alternatives using optimal criteria weights.
| NET alternatives | Criteria | Total Score | |||
|---|---|---|---|---|---|
| Technical status (TRL) | Potential Capacity | Cost | Energy Requirement | ||
| (weights) | (0.460) | (0.022) | (0.250) | (0.268) | |
| Biochar | 1.00 | 0.11 | 0.65 | 1.00 | 0.893 |
| BECCS (Combustion) | 1.00 | 0.58 | 0.63 | 0.42 | 0.743 |
| DAC (Artificial Tree) | 0.67 | 1.00 | 0.60 | 0.42 | 0.593 |
| DAC (lime-soda process) | 1.00 | 1.00 | 0.00 | 0.00 | 0.482 |
| Ocean Liming (Calcination) | 0.67 | 0.00 | 0.92 | 0.24 | 0.603 |
| Ocean Liming (Electrochemical splitting) | 0.33 | 0.00 | 0.69 | 0.19 | 0.375 |
| Enhanced weathering | 0.00 | 0.00 | 1.00 | 0.16 | 0.293 |
The final NET rankings.
| Alternatives | Performance | Ranking | Validation | Ranking from Validation | |
|---|---|---|---|---|---|
| Optimal | Sub-optimal | ||||
| Biochar | 0.893 | 0.886 | 1 | 0.766 | 1 |
| BECCS (Combustion) | 0.743 | 0.736 | 2 | 0.689 | 2 |
| DAC (Artificial Tree) | 0.593 | 0.586 | 4 | 0.639 | 3 |
| DAC (Lime-soda Process) | 0.483 | 0.432 | 5 | 0.477 | 5 |
| Ocean Liming (Calcination) | 0.603 | 0.641 | 3 | 0.528 | 4 |
| Ocean Liming (Electrochemical Splitting) | 0.375 | 0.408 | 6 | 0.342 | 6 |
| Enhanced Weathering | 0.293 | 0.357 | 7 | 0.312 | 7 |