| Literature DB >> 32548327 |
Abstract
In the current green concrete structures, recycled concrete aggregate is used as recycled concrete waste. In this process, concrete waste is collected and crushed using a recycling procedure in order to produce crushed concrete which is then used in structural concrete where it replaces natural aggregate which is coarse. The recycled aggregate concrete is a sustainable concrete waste which in the long term can replace the demand for natural aggregate, a process which would, in turn, lead to its preservation. However, most concrete industries have been observed to be reluctant in the production of recycled aggregate concrete and utilization in its maximum potential. Industries are yet to embrace it not only due to its uncertain material performance but also due to its unexplored manufacturing plant operations which are yet to be established. This research aims to use of a cost-benefit analysis model of the production of ready-mixed high-performance concrete made with recycled concrete aggregate in Thailand. The model focuses on the evaluation of the financial effects which favor the recycled aggregate concrete manufacturing operations instead of the ordinary concrete. Research findings indicate that regardless of the manufacturing plant used, the price of recycled concrete aggregate cannot decrease below the price of natural aggregate concrete. The key result of this research is that recycled concrete aggregate manufacturing set-ups can be used in the industrial-scale manufacture of recycled concrete and at low prices. In addition, overhead bin type and front-end loader type of plants can be used to lower the incremental costs of recycled concrete aggregate. However, the demand and supply factors and the pricing effects of recycled concrete pose various difficulties which are hardly accounted for.Entities:
Keywords: Civil engineering; Cost-benefit analysis; Energy; Front-end loader plant; Industrial engineering; Overhead bin plant; Ready-mixed concrete; Recycled aggregate concrete; Recycled concrete aggregate; Systems engineering
Year: 2020 PMID: 32548327 PMCID: PMC7284077 DOI: 10.1016/j.heliyon.2020.e04135
Source DB: PubMed Journal: Heliyon ISSN: 2405-8440
Figure 1(a) Aggregate unloading to OB plant and (b) aggregate feeding in FEL plant.
Figure 2Estimation of RCA incremental price (Adapted from Wijayasundara et al., 2016). (With permission from Elsevier (Copyright © 2016 Elsevier)).
Process elements and their indirect cost (Wijayasundara et al., 2016).
| Element Number | Element Description | Apportionment Basis |
|---|---|---|
| 1 | Management | RCA volume |
| 2 | Customer and logistic services | RCA trucks requested |
| 3 | Maintenance | RCA volume |
| 4 | Finance | RCA sales revenue |
| 5 | Procurement | RCA volume |
| 6 | Quality control | RCA volume |
| 7 | Information technology (IT) | RCA sales revenue |
| 8 | New projects and upgrades | RCA volume |
| 9 | Administration and utilities | RCA volume |
Figure 3Steps in the ABC approach (Adapted from Wijayasundara et al., 2016). (With permission from Elsevier (Copyright © 2016 Elsevier)).
RMC manufacturing plants.
| Plant number | Category | Operator number | Annual output in m3 | Type |
|---|---|---|---|---|
| 1 | RMC | 3 | 150,000 | Recycling plant |
| 2 | RMC | 2 | 45,000 | Recycling plant |
| 3 | RMC | 1 | 85,000 | FEL |
| 4 | RMC | 2 | 30,000 | FEL |
| 5 | RMC | 1 | 80,000 | FEL |
| 6 | RMC | 2 | 100,000 | OB |
| 7 | RMC | 1 | 150,000 | OB |
| 8 | RMC | 2 | 180,000 | OB |
Estimation of preprocessing costs.
| Plant number | Unit | Description | Amount |
|---|---|---|---|
| 7 | Hour | Operational hours for handling additional materials | 10 |
| 7 | USD per hour | Cost of material handling labor | 55 |
| 7 | USD or MT | Number of days operated | 275 |
| 7 and 8 | Hour | Hours of quality control for each 1000 MT of product | 6 |
| 7 and 8 | USD per hour | Hours of quality control for each 1000 MT of product | 50 |
| 7 and 8 | USD per month | Extra cost of testing | 950 |
| 8 | USD | Scrap value | 0 |
| 8 | Years | Useful life | 40 |
| 8 | % | Coarse RCA yielded from crushed concrete | 75 |
| 8 | % | Utilization of the premises manufacturing crushed concrete | 65 |
| 8 | MT per hour | Hourly capacity depending on upgrade | 120 |
| 8 | USD | Upgrade cost | 550,000 |
| 8 | USD or MT | Additional screening cost | 5 |
Mix compositions of first and second MCB_1 and MCB_2.
| Mix number: | - | 1 | 2 | 3 | 4 | 5 | 6 | 7 | 8 | 9 | 10 | 11 | 12 |
| RCA replacement (% wt.): | - | 0 | 0 | 20 | 20 | 40 | 40 | 60 | 60 | 80 | 80 | 100 | 100 |
| RCA strength (MPa) | - | 65 | 65 | 62 | 62 | 60 | 60 | 58 | 58 | 55 | 55 | 50 | 50 |
| First MCB | Type 1 Cement (kg/m3) | 665 | 665 | 630 | 630 | 605 | 605 | 582 | 582 | 545 | 545 | 500 | 500 |
| Water (kg/m3) | 125 | 125 | 125 | 125 | 125 | 125 | 125 | 125 | 125 | 125 | 125 | 125 | |
| FA (kg/m3) | 818 | 770 | 834 | 783 | 842 | 793 | 852 | 802 | 867 | 816 | 885 | 833 | |
| NA (kg/m3) | 851 | 840 | 694 | 694 | 525 | 557 | 356 | 376 | 181 | 191 | 0 | 0 | |
| RCA (kg/m3) | 0 | 0 | 173 | 173 | 350 | 376 | 534 | 564 | 724 | 766 | 925 | 978 | |
| Silica fume (kg/m3) | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | |
| Superplasticizer (liters/m3) | 7.1 | 7.1 | 6.6 | 6.6 | 6.4 | 6.4 | 6.2 | 6.2 | 5.8 | 5.8 | 5.0 | 5.0 | |
| Second MCB | Type 1 Cement (kg/m3) | 603 | 603 | 563 | 575 | 545 | 553 | 527 | 539 | 497 | 507 | 458 | 465 |
| Water (kg/m3) | 125 | 125 | 125 | 125 | 125 | 125 | 125 | 125 | 125 | 125 | 125 | 125 | |
| FA (kg/m3) | 809 | 786 | 830 | 801 | 832 | 795 | 871 | 802 | 879 | 827 | 885 | 833 | |
| NA (kg/m3) | 839 | 856 | 702 | 716 | 530 | 565 | 359 | 376 | 183 | 193 | 0 | 0 | |
| RCA (kg/m3) | 0 | 0 | 176 | 179 | 356 | 374 | 538 | 564 | 732 | 772 | 925 | 978 | |
| Silica fume (kg/m3) | 71 | 62 | 67 | 55 | 60 | 52 | 55 | 43 | 48 | 38 | 42 | 35 | |
| Superplasticizer (liters/m3) | 7.3 | 7.2 | 7.0 | 6.8 | 6.7 | 6.6 | 6.5 | 6.3 | 6.1 | 5.9 | 5.3 | 5.1 |
Product composition.
| Plant number | Category | Product strength (MPa) | |||||
|---|---|---|---|---|---|---|---|
| 50 | 55 | 58 | 60 | 62 | 65 | ||
| 1 | OB | 10 | 55 | 40 | 15 | 15 | 10 |
| 2 | OB | 40 | 45 | 20 | 15 | 10 | 5 |
| 3 | Front-end | 60 | 30 | 15 | 5 | 0 | 0 |
| 4 | Front-end | 30 | 30 | 20 | 5 | 15 | 5 |
| 5 | Front-end | 35 | 30 | 20 | 5 | 15 | 5 |
Impacted processes as a result of the manufacturing.
| No. | Process | Dir1 | Dir2 | Dir3 | Ind1 | Ind2 | Ind3 | Ind4 | Ind5 | Ind6 | Ind7 | Ind8 | Ind9 |
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| 1 | RCA receipt | ||||||||||||
| 2 | Quality control | ∗ | ∗ | ∗ | ∗ | ∗ | |||||||
| 3 | Storage conveyance | ∗ | ∗ | ∗ | ∗ | ||||||||
| 4 | Storage | ∗ | ∗ | ∗ | |||||||||
| 5 | Mixing conveyance | ∗ | |||||||||||
| 6 | Dry mixing | ||||||||||||
| 7 | Wet mixing | ∗ | |||||||||||
| 8 | Transportation | ||||||||||||
| 9 | Unloading | ||||||||||||
| 10 | Truck return |
Figure 4Increase in RCA cost.
Approximating the processing incremental cost.
| Plant No. | Process | Dir | Ind | Description | Unit | Amount |
|---|---|---|---|---|---|---|
| 1 | 4 | 3 | 3 | Cost of maintenance | USD per year | 2500 |
| 2 | 3 | 3 | Consumption of diesel | 1 per year | 2000 | |
| 3 | 4 | 9 | Cost of constructing storage bin | USD | 60,000 | |
| 4 | 7 | 3 | Mixer power | Watts | 427 |
UIPC for FEL and OB plants.
| Plant type | FEL | OB | ||||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|
| RCA replacement | 0% | 20% | 40% | 60% | 80% | 100% | 0% | 20% | 40% | 60% | 80% | 100% |
| (Process) 1 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 |
| 2 | 0 | 0.48 | 0.53 | 0.64 | 0.69 | 0.73 | 0 | 0.23 | 0.29 | 0.33 | 0.37 | 0.44 |
| 3 | 0 | 0.06 | 0.06 | 0.07 | 0.07 | 0.08 | 0 | 6.05 | 6.12 | 6.29 | 6.31 | 6.37 |
| 4 | 0 | 0.07 | 0.21 | 0.25 | 0.29 | 0.33 | 0 | 0.05 | 0.07 | 0.15 | 0.18 | 0.21 |
| 5 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 |
| 6 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 |
| 7 | 0 | 0.12 | 0.13 | 0.13 | 0.13 | 0.12 | 0.13 | 0.12 | 0.13 | 0.13 | 0.13 | |
| 8 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 |
| 9 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 |
| (Process) 10 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 | 0 |
Figure 5Breakdown of unit incremental price in FEL type plant for 60 MPa using MCB_2 scenario.
Figure 6Breakdown of unit incremental price in OB type plant for 60 MPa using MCB_2 scenario.
The key parameter's standard deviation and mean.
| Parameter | Units | MCB first scenario | MCB second scenario | ||
|---|---|---|---|---|---|
| Mean | Standard deviation | Mean | Standard deviation | ||
| Content of supplementary cement | kg/m3 | 415 | 81 | 380 | 66 |
| Composition of RCA | % | 65 | 0.3 | 55 | 0.4 |
| Distance to transport RCA | kilometers | 32.4 | 6.2 | 40.5 | 5.3 |
| RCA additional processing cost | USD per MT | 4.3 | 0.2 | 3.9 | 0.5 |
| Inward bound CC price | USD per MT | 36.9 | 4.4 | 25.8 | 3.7 |
RCA incremental price range.
| RCA replacement (%) | FEL | OB |
|---|---|---|
| 20 | 0 to 7.5 | 5.5 to 16.0 |
| 40 | 7.5 to 9.5 | 7.5 to 16.5 |
| 60 | 8.5 to 10.5 | 9.5 to 17.5 |
| 80 | 4.5 to 12.5 | 9.5 to 18.0 |
| 100 | 5.5 to 12.0 | 9.0 to 18.0 |