Keywords

1 Introduction

Nowadays, the assembled product, such as vacuum cleaner and smartphone is delivered to users through a global supply chain that spans procurement, manufacturing, and sales in multiple countries [1]. The economic activities such as those have caused the Marine-Plastic-Issue and global warming [2]. The Marine-Plastic-Issue is caused by disposing End-of-Life (EOL) product made from plastic materials, and global warming is occurred by Greenhouse Gas (GHG) emission in manufacturing. In order to resolve their problems, governments and manufacturing companies are taking action in around the world. For example, EU adopt the low “the reduction of impact of certain plastic products on the environment” in 2018 and decided to ban the single-used plastic products, which was not recycled, such as straw and cutlery by 2021 [3]. The Coca-Cola Company announced that they would collect as much cans and plastic bottles as the world's product sales volume by 2030 [4]. Japanese government took effect with the plastic regulation and announced that GHG emissions became zero by 2050 [2]. In order for manufacturing companies to develop sustainability, they are required to design the Global Closed-Loop Supply Chain (GCLSC) network for reducing GHG emissions and recycling EOL products in manufacturing stages [5].

The GCLSC integrates the global supply chain network [6], which is a series of cross-border transaction of products, and the local reverse supply chain network [7], which is a local transaction for collecting and recycling EOL products because as accordance with the Basel Convention [8], the collection center, the recovery facility, and the disposal facility must be located in the same country as the place of market. However, GCLSC network is costly for procurement, manufacturing, transportation, recycling and opening facilities costs. Thus, the decision maker who designs configuration of GCLSC network should consider to select appropriate global suppliers considering material-based GHG emissions because the amount of material-based GHG emissions in products is dependent on power generation methods such as thermal power generation, hydroelectricity, and solar photovoltaics in each country [6]. As a previous study, Armin et al. [9] proposed CLSC model to determine facility location decisions and lateral transshipment quantities that minimize the total supply chain cost across different disruption scenarios. However, they did not evaluate the environmental impacts such as recycling rate and GHG emissions. Aldoukhi and Gupta [10] designed CLSC considering to minimize total cost and carbon emission and to maximize service level of retailers. However, they did not consider materials such as plastic and aluminum obtained from recycling EOL product. Polat et al. [11] integrated forward and reverse logistics network design. However, they did not take into account that different countries have different costs and GHG emissions when procuring and manufacturing components.

This study designs the GCLSC network to (1) minimize total cost and (2) maximize the entire recycling rate by Integer Programming (IP) [12] with ε constraint for entire recycling rate on global supply chain network and domestic closed-loop, where the GHG emission from components procurement and the GHG saving weight by recycling EOL product is calculated. First, the GCLSC network is draw and modeled. Next, the objective functions for minimizing total cost and the environmental evaluation for entire recycling rate and GHG emission are formulated with IP [12]. Finally, a numerical experiment is conducted and evaluated in terms of costs, entire recycling rate, and material-based GHG emission weight.

2 Model

2.1 Assumption and Notation

Figure 1 shows a GCLSC network model proposed in this study. That integrates a global supply chain network [6] and a local reverse supply chain network [7]. In the global supply chain network, the component j is procured from supplier o and transported to factory p for manufacturing an assembly product. After that, the assembly product is transported from factory p to market q. In the market q, assembly product is sold to an user and returned by the user as the EOL product. When component j is procured from supplier o, the material-based GHG emission GHGoj is generated, and the amount of it is depends on the country where supplier o is in.

Fig. 1
A flowchart depicts the global supply chain network with G H G emissions of 3 countries, leading to the local supply chain network with transportation costs via the market.

Global closed-loop supply chain network model: Case of 3 countries

In the local reverse supply chain network, EOL products are transported from market q to collection center g. In a collection center g, EOL products are identified and divided status s based on user situation. Furthermore, EOL product with status s is transported from collection center g to recovery facility r or disposal facility h. When the EOL product is transported to recovery facility, it is recycled based on EOL product status s. On the other hand, when the EOL product is transported to disposal facility, it is disposed.

In this study, material-based GHG emission by each material GHGoj for component j is different based on procured country from supplier o. Moreover, recycling cost RCs, recovered material weight RWs, and GHG saving weight GHGs and by recycling EOL product is dependent on the status s. The recycling cost RCs includes disassembly, processing and disposal costs. The disassembly cost is based on disassembly time by Recyclability Evaluation Method (REM) [13]. The processing cost relates to shredding and so on. The disposal cost is the sum of final processing cost such as landfill and sale of recycling material. The recovered material weight RWs means the recovered material weight by recycling EOL product.

The notations used in this study are as follows:

Sets:

O:

Set of suppliers, o  ∈  O

J:

Set of components, j  ∈  J

P:

Set of factories, p  ∈  P

Q:

Set of markets, q  ∈  Q

G:

Set of collection centers, g  ∈  G

R:

Set of recovery facilities, r  ∈  R

H:

Set of disposal facilities, h  ∈  H

S:

Set of statues of EOL product, s  ∈  S

Variables:

vopj:

Amount of components j transported from supplier o to factory p

vpq:

Amount of products transported from factory p to market q

vqg:

Amount of EOL products transported from market q to collection center g

vgrs:

Amount of EOL products with status s transported from collection center g to recovery facility r

vghs:

Amount of EOL products with status s transported from collection center g to disposal facility h

up:

1 if the fixed opening cost at factory p is opened, and 0 otherwise

ur:

1 if the fixed opening cost at recovery facility r is opened, and 0 otherwise

TC:

Total cost [US$]

TGC:

Total cost of global supply chain network [US$]

TRC:

Total cost of local reverse supply chain network [US$]

RR:

Entire recycling rate of local reverse supply chain network [%]

\(\varepsilon_{RR}\):

Epsilon rate of entire recycling rate [%]

TGHG:

Total GHG emission on global GCLSC [g-CO2eq]

GHGoj:

GHG emission weight for component j procured from supplier o [g-CO2eq]

GHGs:

GHG saving weight by recycling EOL product with status s [g-CO2eq]

Parameters:

LCop:

Transportation cost of a component from supplier o to factory p [US$]

LCpq:

Transportation cost of a product from factory p to market q [US$]

LCqg:

Transportation cost of a EOL product from market q to collection center g [US$]

LCgr:

Transportation cost of a EOL product collection center g to recovery facility r [US$]

LCgh:

Transportation cost of a EOL product collection center g to disposal facility h [US$]

PCoj:

Procurement cost of component j by supplier o [US$]

MCop:

Manufacturing cost per product at factory p [US$]

RCs:

Recycling cost per EOL product with status s [US$]

FCp:

Fixed cost for opening factory p [US$]

FCr:

Fixed cost for opening recovery facility r [US$]

RWs:

Recovered material weight of EOL product with status s [g]

PW:

Total weight of a EOL product [g]

2.2 Formulation

This GCLSC model has a bi-objective problem for minimizing total cost TC and for maximizing the entire recycling rate RR. Regarding the total cost TC on GCLSC network, Eq. (1) minimizes of total cost of global supply chain network TGC and local reverse supply chain network TRC. Equation (2) maximizes the entire recycling rate RR on GCLSC network which is the ratio of total recovered material weight of recycling EOL product at recovery facilities against the total collected material weight of collecting EOL product at collection centers. Equation (3) means the total cost of global supply chain TGC including the procurement cost PCoj for component j from supplier o, the manufacturing cost MCp of product in factory p, the opening factory cost FCp for assembly factory p, and the transportation cost LCop and LCpq transported from supplier o to factory p and from factory p to market q. Equation (4) represents the total cost of local reverse supply chain network TRC including the recycling cost RCs for recycling EOL product with status s, the opening facility cost FCr for recovery facility r, and the transportation cost LCqg, LCgr, and LCgh transported from market q to collection center g and from collection center g to recovery facility r or disposal facility h. Equation (5) is epsilon constraint of entire recycling rate RR for GCLSC network. Equation (6) shows the total GHG emission TGHG which is the difference between the sum of GHG emission weight GHGoj for procured component j minus the sum of GHG saving weight GHGs for recycled EOL product with status s.

Objective functions and GHG evaluation:

$$TC = TGC + TRC{ } \to {\text{min}}$$
(1)
$$RR = \frac{{\mathop \sum \nolimits_{g \in G}^{G} \mathop \sum \nolimits_{r \in R}^{R} \mathop \sum \nolimits_{s \in S}^{S} RW_{s} v_{grs} }}{{\mathop \sum \nolimits_{q \in Q}^{Q} \mathop \sum \nolimits_{g \in G}^{G} TWv_{pq} }} \to {\text{max}}$$
(2)
$$\begin{aligned} TGC & = \mathop \sum \limits_{{o \in O}}^{O} \mathop \sum \limits_{{p \in P}}^{P} \mathop \sum \limits_{{j \in J}}^{J} (PC_{{oj}} + ~LC_{{op}} )v_{{opj}} + \mathop \sum \limits_{{p \in P}}^{P} \mathop \sum \limits_{{q \in Q}}^{Q} \left( {LC_{{pq}} + MC_{p} } \right)v_{{pq}} \\ & \quad + \mathop \sum \limits_{{p \in P}}^{P} FC_{p} u_{p} \\ \end{aligned}$$
(3)
$$\begin{aligned} TRC & = \mathop \sum \limits_{{q \in Q}}^{Q} \mathop \sum \limits_{{g \in G}}^{G} LC_{{qg}} v_{{qh}} + \mathop \sum \limits_{{g \in G}}^{G} \mathop \sum \limits_{{r \in R}}^{R} \mathop \sum \limits_{{s \in S}}^{S} \left( {RC_{s} + LC_{{gr}} } \right)v_{{grs}} \\ & \quad + \mathop \sum \limits_{{g \in G}}^{G} \mathop \sum \limits_{{h \in H}}^{H} \mathop \sum \limits_{{s \in S}}^{S} LC_{{gr}} v_{{grh}} + \mathop \sum \limits_{r}^{R} FC_{r} u_{r} \\ \end{aligned}$$
(4)
$$RR \, { \geqq } \, \varepsilon_{RR}$$
(5)
$$TGHG = \mathop \sum \limits_{o \in O}^{O} \mathop \sum \limits_{p \in P}^{P} \mathop \sum \limits_{j \in J}^{J} GHG_{oj} v_{opj} - \mathop \sum \limits_{g \in G}^{G} \mathop \sum \limits_{r \in R}^{R} \mathop \sum \limits_{s \in S}^{S} GHG_{s} v_{grs}$$
(6)

3 Problem Example

To design the GCLSC network, a problem example is prepared to integrate a global supply chain and local reverse supply chain. A vacuum cleaner with 23 types of components is used as examples of assembled and EOL product as well as Hayashi et al. [14], Ijuin et al. [7], and Ishii et al. [15]. It is assumed that a motor in vacuum cleaner is excluded because the procurement cost of the motor is about 95% of the sum of procured components for all the components. The details of GCLSC example are prepared in this study as follows.

  • As suppliers, 52 cities are set from 4 country for China, Malaysia, the United States, and Japan, in other word, each country has 13 suppliers.

  • As candidate factories’ location, 4 cities for Shanghai, Kuala Lumpur, Seattle, and Tokyo, are selected. The production capacity of each factory is 6,000 units, and the market demand set at Tokyo, the Japan, is 12,000 units.

  • As collection centers, 3 sites in Itabashi, Koto, and Ota where are in Japan, are prepared.

  • As recovery facilities for recycling EOL product, 3 sites in Ota, Chiba, and Chofu where are in Japan, are selected. They have recyclable capability based on status s of EOL product.

  • As disposal facility, Koto site where is in Japan, is prepared.

The statuses of EOL products in the case of vacuum cleaner are also prepared based on disassembly scenarios [13]. From disassembly scenarios, the recycling cost RCs and recovered material weight RWs, and GHG saving weight GHGs are divided 4 statuses. For example, the EOL product with status number #4 has 1.53 [US$] for recycling cost, 952.79 [g] recovered material weight, and 1276.94 [g-CO2eq] GHG saving weight by recycled components in EOL product and it is recycled in recovery facility in Chiba or Ota.

4 Result

To solve the bi-objective problem for minimizing total cost and maximizing the entire recycling rate, the entire recycling rates RR between from 0 [%] (minimum) to 60 [%] (maximum) are changed by epsilon constraint \(\varepsilon_{RR}\). Figure 2 shows the total cost and the total material-based GHG emission of GCLSC network with the entire recycling rate RR. The sum of manufacturing cost and procurement cost was the highest, accounting for over 90% of the total cost. Even if any target recycling rate were set, the total transportation cost on global supply chain, the total procurement cost, the total manufacturing cost, and total opening facility cost for assembly factories were not changed in the all cases. Because of that, the entire recycling rate can not impact on the global supply chain in the example. On the other hand, the total transportation cost on the local reverse supply chain, the total recycling cost and the total opening facility cost were increased. One of the reasons was that lager amount of EOL products was recycled in attempting to increase the entire recycling rate.

Fig. 2
A stacked bar graph of total cost versus the entire recycling rate for various factors. The total G H G emissions are denoted by a decreasing line in the graph.

Total cost and total GHG emission of GCLSC with entire recycling rate

From Fig. 2, when the entire recycling rate was increased by 20 [%], the total GHG emission was decreased by 6,000 [kg-CO2eq]. This is because weight of recovered materials was less GHG emission than procuring virgin one. Therefore, it is found that GHG emissions could be lower at the same time as increasing the recycling rate.

Figure 3 shows the GCLSC network in the case with the maximal entire recycling rate (60 [%]). In the case, Chinese and Malaysian suppliers were selected. Additionally, from Fig. 2, 92% of the total cost was occupied by total manufacturing cost and total procurement cost. Therefore, candidate locations with lower procurement and manufacturing cost, such as suppliers and factories in China and Malaysia, were selected.

Fig. 3
A G C L S C network of the countries China, Japan, and Malaysia with different legends for various location types and transportation items.

GCLSC network flow of component, product, and EOL products with the maximal entire recycling rate (60 [%]) (Map source: https://www.freemap.jp/)

On the other hand, Chiba’s recovery facility in Japan whose opening cost was the highest in the candidate locations is opened. One of the reasons is that was the recovery facilities in Ota and Chofu can not recycle the EOL products with statuses 1 (All components disassembled) and 2 (Recycling rate maximum) assumed as in this study. In order to increase the entire recycling rate, all EOL products were transported and recycled in Chiba’s recovery facility in the case.

5 Conclusion

This study designed the GCLSC network and observed changes of the costs, entire recycling rate, total GHG emission, and network flow for component, product and EOL product.

In the GCLSC network, costs in global forward supply chain such as component procurement and manufacturing product was by 9 times higher than ones in the local reverse supply chain. Thus, total GHG emission was decreased because larger amount of EOL products were recycled when the entire recycling rate is increased. In the global supply chain flow, suppliers and factory were selected in China and Malaysia for saving procurement cost and manufacturing cost. On the other hand, as a local reverse supply chain flow, Chiba’s recovery facility which had the highest opening was opened in order to increase the entire recycling rate.

Further studies should consider a multi-objective model to minimizing cost, to maximize recycling rate, and to minimize GHG emission simultaneously.