Green Activity-Based Costing Production Decision Model for Recycled Paper
Abstract
:1. Introduction
2. Sustainable Management under Green Paper Industry
2.1. Green Innovation in Paper Industry
2.2. MIP Model for Green Paper Industry
2.3. ABC and TOC
3. Problem Statement and Model Formulation
3.1. The Objective Function
3.2. Revenue of Main Products and Byproducts
3.3. Direct Material and Expense
3.4. Unit-Level Activity Cost
3.5. Direct Labor Cost
3.6. Batch-Level Activity Cost
3.7. Product-Level Activity Cost
3.8. Machine Cost
3.9. Benefit of Using RDF-5
4. Numerical Example
4.1. Description of the Case Problem
4.2. Analysis
4.3. Sensitivity Analysis
5. Discussion
5.1. Managerial Implications
5.2. Limitations
6. Conclusions
Author Contributions
Funding
Acknowledgments
Conflicts of Interest
Notations
Corporate profit; | |
Xi | Quantity of product i; |
Unit price of product i; | |
cs | Unit price of byproduct s |
bis | The quantity of byproduct s of one unit of product i |
Saved pth steam costs, when p = 1, the preferential rate is applicable; when p = 2, the basic preferential rate is applicable; when p = 3, the excess rate is applicable; | |
Saved pth steam machine hours, when p = 1, the preferential rate is applicable; when p = 2, the basic preferential rate is applicable; when p = 3, the excess rate is applicable; | |
Saved qth electric power costs, when q = 1, the preferential rate is applicable; when q = 2, the basic preferential rate is applicable; when q = 3, the excess rate is applicable; | |
Saved qth generating machine hours, when q = 1, the preferential rate is applicable; when q = 2, the basic preferential rate is applicable; when q = 3, the excess rate is applicable; | |
Saved activity driver demands of unit-level activity j (j ∈ U) for steam machine hours of one-unit product i; | |
Saved activity driver demand of unit-level activity j (j ∈ U) for generating machine hours of one-unit product i; | |
Unit cost of mth raw material; | |
Unit cost of mth raw material; mth raw material demand of one-unit product I; | |
Available quantity of raw material Q. | |
Running activity cost per activity driver for activity j; | |
Activity driver demand of unit-level activity j (j ∈ U) of one-unit product i; | |
Total direct labor cost in (see Figure 2); | |
Total direct labor cost in (see Figure 2); | |
Total labor hours needed for the company; | |
Upper limit of total direct labor hours of normal work (see Figure 2); | |
Upper limit of total direct labor hours including overtime work (see Figure 2); | |
The quantity of resource used by each batch-level activity j (j ∈ B) for product i; | |
The number of batches for batch-level activity j (j ∈ B) used by product i; | |
The quantity of product i for each batch-level activity j (j ∈ B); | |
The quantity available for the activity driver of batch-level activity j (j ∈ B). | |
Demand of activity driver needed by product-level activity j (j ∈ P) for product i; | |
Production indicator of product i; If (Ri = 1), then product i will be produced. Otherwise, (Ri = 0); | |
Maximum demand for product i; | |
The quantity available for the activity driver of activity j (j ∈ P). | |
Total machine cost in (see Figure 3); | |
Machine hours of kth level capacity (see Figure 3); | |
SOS1 set of 0–1 variables (special order of the first kind), where one and only one variable must be nonzero; = 1 means that machine hour is expanded to . | |
Machine hour demand for one unit of product i; | |
Environmental management cost; | |
Processed gas p; | |
The total quantity of gas p from product i.; | |
G | The quantity of carbon equivalent of various gases allowed to be emitted from the mill paper-making process. |
Appendix A
Z = [(income from main paper products) + (relevant byproducts) + (saved electric power cost) + (saved steam cost)] − [(unit-level activity cost: total material cost + total expense + total direct labor cost+ total machine cost) + (batch-level activity cost) + (product-level activity cost) + (total facility-level activity cost) + environmental management cost] | ||
=(320 + 280 + 250) + {[0.8*(5 + 6 + 7)] + [0.5*( + 2 + 3)] + [0.035*(10 + 12 + 15)] + [0.02*(10 + 12 + 15)] + [0.2*(23 + 25 + 30)] + [0.05*(23 + 25 + 30)] + [0.7*(23 + 25 + 30)]} + (92,000 + 101,200 + 108,100) + (32,000 + 35,200 + 37,600) − {[(20*3 + 15*4 + 5*2) + (20*2 + 15*3 + 5*4) + (20*1 + 15*2 + 5*7)] + [(1*10 + 2*23) + (1*12 + 2*25) + (1*15 + 2*30)] + (38,204 + 62,082) + [(6*1) + (6*2) + (6*3)] + [(14*2) + (14*3) + (14*4)] + (2*3) + (2*4) + (2*5)] + [(1*2) + (1*2) + (1*3)] + [(100*15) + (100*12) + (100*18)] + (85,600 + 98,975 + 115,025) + 20,000 = 160.9 + 143.21 + 126.425 + 92,000 + 101,200 + 108,100 + 32,000 + 35,200 + 37,600 − 38,204 − 62,082 − 85,600 − 98,975 − 115,025 − 6 − 12 − 18 − 28 − 42 − 56 − 6 − 8 − 10 − 2 − 2 − 3 − 1500 − 1200 − 1800 − 20,000 | ||
Subject to: | ||
Raw material and expense constraints: | Stepwise facility-level machine hour constraints: Direct labor constraints: | Batch-level production activity constraints: Batch-level preparation activity constraints: |
Batch-level treatment activity constraints: | Batch-level cutting activity constraints: Product-level constraints: Saved electric power cost = Constraints: Saved steam cost = Constraints: | Estimated data of different gases emitted from the mill paper-making process: NOx: 0.0006*(23 + 25 + 30) CO2: 0.54*(23 + 25 + 30) SO2: 0.0000024*(23 + 25 + 30) CO: 0.00012*(23 + 25 + 30) COD: 0.0009*(23 + 25 + 30) BOD: 0.00006*(23 + 25 + 30) SS: 0.000075*(23 + 25 + 30) AOX: 0.0000009*(23 + 25 + 30) In order to conform to the environmental protection policy, the carbon equivalent of the company should not exceed 80,000 units. |
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(a) Example Data | ||||||||
---|---|---|---|---|---|---|---|---|
Data Category | Index & Activity-Driver | Activity | Parameter | Product 1 | Product 2 | Product 3 | Available Capacity | |
Selling price | j | pi | 320 | 280 | 250 | |||
Unit cost/price | ||||||||
Material (Unit-level) | m = 1(pulp substitute) | $20.00/unit | ai1 | 3 | 2 | 1 | Q1 = 11,310 | |
m = 2(cleanable waste paper) | $15.00/unit | ai2 | 4 | 3 | 2 | Q2 = 17,020 | ||
m = 3(ordinary waste paper) | $5.00/unit | ai3 | 2 | 4 | 7 | Q3 = 24,750 | ||
Expense | m = 4(water) | $1.00/unit | ai4 | 10 | 12 | 15 | Q4 = 70,400 | |
m = 5(coal) | $2.00/unit | ai5 | 23 | 25 | 30 | Q5 = 147,960 | ||
Selling byproduct | s = 1(electricity) | $0.80/unit | bi1 | 5 | 6 | 7 | ||
s = 2(steam) | $0.50/unit | bi2 | 1 | 2 | 3 | |||
s = 3(organic compost) | $0.035/unit | bi3 | 10 | 12 | 15 | |||
s = 4(cement products) | $0.02/unit | bi4 | 10 | 12 | 15 | |||
s = 5(building materials) | $0.20/unit | bi5 | 23 | 25 | 30 | |||
s = 6(reinforced structural building materials) | $0.05/unit | bi6 | 23 | 25 | 30 | |||
s = 7(fireplates) | $0.70/unit | bi7 | 23 | 25 | 30 | |||
Unit-level activity | Machine hours | 1 | λi1 | 6 | 7 | 8 | ||
Labor hours | 2 | λi2 | 4 | 5 | 6 | |||
RDF5 saved cost | Electric energy | 3 | λi3 | 5 | 6 | 7 | ||
Steam (heat) energy | 4 | λi4 | 1 | 2 | 3 | |||
Batch-level activity | Activity-driver | Cost per activity driver | ||||||
Pulping | Blending | $6 | 5 | αi5 μi5 | 1 3 | 2 2 | 3 1 | T5 = 7750 |
Papermaking | Papermaking | $14 | 6 | αi6 μi6 | 2 8 | 3 6 | 4 3 | T6 = 12,470 |
Coating | Treatment | $2 | 7 | αi7 μi7 | 3 5 | 4 4 | 5 3 | T7 = 6100 |
Packing | Packing | $1 | 8 | αi8 μi8 | 2 3 | 2 2 | 3 1 | T8 = 5400 |
Product-level activity-Design | Drawings | $100 | 9 | ρi9 | 15 | 12 | 18 | D6 = 50 |
Maximum demand | Vi | 2000 | 2500 | 3000 | ||||
(b) Example data—facility level cost | ||||||||
Environmental Management Cost | Total Cost | $20,000 | ||||||
Machine hours constraint-Cost | MC0 = $85,600 | MC1 = $98,975 | MC2 = $115,025 | |||||
Machine hours | MH0 = 42,800 | MH1 = 48,150 | MH2 = 53,500 | |||||
Machine cost rate | mr0 = $2/h | mr1 = $2.5/h | mr2 = $3/h | |||||
Direct labor constraint-Cost | LC1 = $38,204 | LC2 = $62,082 | ||||||
Labor hours | LH1 =19,102 | LH2 = 28,653 | ||||||
Wage rate | wr1 = $2/h | wr2 = $2.5/h | ||||||
Power constraint | ||||||||
Cost | SEC1 = $92,000 | SEC2 = $101,200 | SEC3 = $108,100 | |||||
Hour | SGH1 = 36,800 | SGH2 = 41,400 | SGH3 = 46,000 | |||||
Rate | PT1 = $2.5/10 thousand kWh | PT2= $2/10 thousand kWh | PT3 = $1.5/10 thousand kWh | |||||
Steam(heat) constraint | ||||||||
Cost | SSC1 = $32,000 | SSC2 = $35,200 | SSC3 = $37,600 | |||||
Hour | SSH1 = 12,800 | SSH2 = 14,400 | SSH3 = 16,000 | |||||
Rate | ST1 = $2.5/10 thousand kWh | ST2 = $2/10 thousand kWh | ST3 = $1.5/10 thousand kWh |
Symbol | Value | Symbol | Value | Symbol | Value | Symbol | Value |
---|---|---|---|---|---|---|---|
Z | $643,193.80 | 1250 batches | CO2 | 65,620.8 t | 0 | ||
1940 t | 480 batches | SO2 | 0.291648 t | 0 | |||
2500 t | 243 batches | CO | 14.5824 t | 0.577217 | |||
480 t | 417 batches | COD | 109.368 t | 0.422783 | |||
$22,448.00 | 160 batches | BOD | 7.2912 t | 0 | |||
$4190.00 | 388 batches | SS | 9.114 t | 1 | |||
$1981.00 | 625 batches | AOX | 0.109368 t | 0 | |||
$1132.00 | 160 batches | 1 | 0 | ||||
$24,304.00 | 647 batches | 1 | 1 | ||||
$6076.00 | 1250 batches | 1 | 0 | ||||
$85,064.00 | 480 batches | 1 | 0 | ||||
647 batches | NOx | 72.912 t | 0 | 1 |
Cost Decrease/Increase Ratio (%) | Profit | Increase/Decrease (Compared with the Initial Value) | Increase Profit | |
---|---|---|---|---|
pulp substitute | −30% | 710,993.8 | 10.54% | 67,800.0 |
pulp substitute | −25% | 699,693.8 | 8.78% | 56,500.0 |
pulp substitute | −20% | 688,393.8 | 7.03% | 45,200.0 |
pulp substitute | −15% | 677,093.8 | 5.27% | 33,900.0 |
pulp substitute | −10% | 665,793.8 | 3.51% | 22,600.0 |
pulp substitute | −5% | 654,493.8 | 1.76% | 11,300.0 |
pulp substitute | 0% | 643,193.8 | 0.00% | 0.0 |
pulp substitute | 5% | 631,893.8 | −1.76% | −11,300.0 |
pulp substitute | 10% | 620,593.8 | −3.51% | −22,600.0 |
pulp substitute | 15% | 609,293.8 | −5.27% | −33,900.0 |
pulp substitute | 20% | 597,993.8 | −7.03% | −45,200.0 |
pulp substitute | 25% | 586,693.8 | −8.78% | −56,500.0 |
pulp substitute | 30% | 575,393.8 | −10.54% | −67,800.0 |
Cost Decrease/Increase Ratio (%) | Profit | Increase/Decrease (Compared with the Initial Value) | Increase Profit | |
---|---|---|---|---|
Cleanable waste paper | −30% | 716,183.8 | 11.35% | 72,990.0 |
Cleanable waste paper | −25% | 704,018.8 | 9.46% | 60,825.0 |
Cleanable waste paper | −20% | 691,853.8 | 7.57% | 48,660.0 |
Cleanable waste paper | −15% | 679,688.8 | 5.67% | 36,495.0 |
Cleanable waste paper | −10% | 667,523.8 | 3.78% | 24,330.0 |
Cleanable waste paper | −5% | 655,358.8 | 1.89% | 12,165.0 |
Cleanable waste paper | 0% | 643,193.8 | 0.00% | 0.0 |
Cleanable waste paper | 5% | 631,028.8 | −1.89% | −12,165.0 |
Cleanable waste paper | 10% | 618,863.8 | −3.78% | −24,330.0 |
Cleanable waste paper | 15% | 606,698.8 | −5.67% | −36,495.0 |
Cleanable waste paper | 20% | 594,533.8 | −7.57% | −48,660.0 |
Cleanable waste paper | 25% | 582,368.8 | −9.46% | −60,825.0 |
Cleanable waste paper | 30% | 570,203.8 | −11.35% | −72,990.0 |
Cost Decrease/Increase Ratio (%) | Profit | Increase/Decrease (Compared with the Initial Value) | Increase Profit | |
---|---|---|---|---|
Ordinary waste paper | −30% | 669,252.8 | 4.05% | 26,059.0 |
Ordinary waste paper | −25% | 664,882.8 | 3.37% | 21,689.0 |
Ordinary waste paper | −20% | 660,512.8 | 2.69% | 17,319.0 |
Ordinary waste paper | −15% | 656,142.8 | 2.01% | 12,949.0 |
Ordinary waste paper | −10% | 651,813.8 | 1.34% | 8620.0 |
Ordinary waste paper | −5% | 647,503.8 | 0.67% | 4310.0 |
Ordinary waste paper | 0% | 643,193.8 | 0.00% | 0.0 |
Ordinary waste paper | 5% | 638,883.8 | −0.67% | −4310.0 |
Ordinary waste paper | 10% | 634,573.8 | −1.34% | −8620.0 |
Ordinary waste paper | 15% | 630,263.8 | −2.01% | −12,930.0 |
Ordinary waste paper | 20% | 625,953.8 | −2.68% | −17,240.0 |
Ordinary waste paper | 25% | 621,643.8 | −3.35% | −21,550.0 |
Ordinary waste paper | 30% | 617,333.8 | −4.02% | −25,860.0 |
Increasing Ratio | Profit | Increase/Decrease (Compared with the Initial Value) | Increase Profit | |
---|---|---|---|---|
Pulp substitute | 0% | 643,193.8 | 0.00% | 0.0 |
Pulp substitute | 5% | 654,512.8 | 1.76% | 11,319.0 |
Pulp substitute | 10% | 654,512.8 | 1.76% | 11,319.0 |
Pulp substitute | 15% | 654,512.8 | 1.76% | 11,319.0 |
Pulp substitute | 20% | 654,512.8 | 1.76% | 11,319.0 |
Pulp substitute | 25% | 654,512.8 | 1.76% | 11,319.0 |
Pulp substitute | 30% | 654,512.8 | 1.76% | 11,319.0 |
Increasing Ratio | Profit | Increase/Decrease (Compared with the Initial Value) | Increase Profit | |
---|---|---|---|---|
Clean waste paper | 0% | 643,193.8 | 0.00% | 0.0 |
Clean waste paper | 5% | 654,512.8 | 1.76% | 11,319.0 |
Clean waste paper | 10% | 654,512.8 | 1.76% | 11,319.0 |
Clean waste paper | 15% | 654,512.8 | 1.76% | 11,319.0 |
Clean waste paper | 20% | 654,512.8 | 1.76% | 11,319.0 |
Clean waste paper | 25% | 654,512.8 | 1.76% | 11,319.0 |
Clean waste paper | 30% | 654,512.8 | 1.76% | 11,319.0 |
Increasing Ratio | Profit | Increase/Decrease (Compared with the Initial Value) | Increase Profit | |
---|---|---|---|---|
Ordinary waste paper | 0% | 643,193.8 | 0.00% | 0.0 |
Ordinary waste paper | 5% | 643,193.8 | 0.00% | 0.0 |
Ordinary waste paper | 10% | 643,193.8 | 0.00% | 0.0 |
Ordinary waste paper | 15% | 643,193.8 | 0.00% | 0.0 |
Ordinary waste paper | 20% | 643,193.8 | 0.00% | 0.0 |
Ordinary waste paper | 25% | 643,193.8 | 0.00% | 0.0 |
Ordinary waste paper | 30% | 643,193.8 | 0.00% | 0.0 |
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Hsieh, C.-L.; Tsai, W.-H.; Chang, Y.-C. Green Activity-Based Costing Production Decision Model for Recycled Paper. Energies 2020, 13, 2413. https://doi.org/10.3390/en13102413
Hsieh C-L, Tsai W-H, Chang Y-C. Green Activity-Based Costing Production Decision Model for Recycled Paper. Energies. 2020; 13(10):2413. https://doi.org/10.3390/en13102413
Chicago/Turabian StyleHsieh, Chu-Lun, Wen-Hsien Tsai, and Yao-Chung Chang. 2020. "Green Activity-Based Costing Production Decision Model for Recycled Paper" Energies 13, no. 10: 2413. https://doi.org/10.3390/en13102413
APA StyleHsieh, C.-L., Tsai, W.-H., & Chang, Y.-C. (2020). Green Activity-Based Costing Production Decision Model for Recycled Paper. Energies, 13(10), 2413. https://doi.org/10.3390/en13102413