CHEMICAL ENGINEERING TRANSACTIONS  
 

VOL. 62, 2017 

A publication of 

 
The Italian Association 

of Chemical Engineering 
Online at www.aidic.it/cet 

Guest Editors: Fei Song, Haibo Wang, Fang He 
Copyright © 2017, AIDIC Servizi S.r.l. 
ISBN 978-88-95608- 60-0; ISSN 2283-9216 

Study on the Life-Cycle Engineering Cost Management of 
Large Chemical Projects 

Yong Gu 
Langfang Teachers University, Langfang 065000, China 
gy_syc@sohu.com 

This paper conducted a study on the life-cycle engineering cost management of large chemical projects, with 
the purpose of standardizing the management process and reducing the costs at all stages. Specifically, the 
LCC analysis method was adopted to analyze the life cycle cost of large-scale chemical engineering projects 
through detailed introduction to the theory, cost structure and cost analysis steps, based on which the all-
factor LCC model of large-scale chemical projects was established. Finally, through the determination of 
constraints, the optimization of the life-cycle engineering cost model for large-scale chemical projects was 
realized. This research is helpful to strengthen the engineering cost management for large-scale chemical 
projects at all stages, and is instructive for the investment decision in large-scale chemical engineering 
projects. 

1. Introduction 
In the context of global economic growth slowing down and commodity prices continuing to fall, the downward 
pressure on the domestic economy has been increasingly growing. And the petroleum and chemical industries 
are facing more and more fierce competition worldwide (Demeulemeester, 2015; Zhong and Zhang, 2006). In 
order to reduce the engineering cost and improve economic efficiency comprehensively, all major 
petrochemical enterprises have paid more attention to the management of engineering costs, so as to reduce 
the life-cycle engineering cots of large-scale chemical projects (Jiang, 2002). 
The schedule, cost, quality and safety of large-scale chemical projects are the four major elements of project 
management, among which cost management is directly related to the project costs (Gluch and Baumann, 
2004). The engineering cost is the manifestation of the monetary cost in all stages of the project, which is 
reflected in the decision-making phase, implementation phase, operations phase and closure phase of the 
large-scale chemical projects (Guo and Zhang, 2015). Although the decision-making phase takes fewer costs 
out of all engineering costs, it affects the total engineering costs by over 90% (Nikolay, 2016). Therefore, it is 
necessary to improve the life-cycle cost management of large chemical projects life cycle, especially during 
the feasibility and design phase (Kirk and Dell'Isola, 1995). 
This paper first gave an overview of the LCC (Life Cycle Costing) theory, analyzed the composition of 
engineering costs in each phase of the project, and then used the LCC method to analyze other factors that 
affect the engineering costs of large-scale chemical projects based on the classic LCC model to established 
an all-factor model for large chemical projects; Finally, the life-cycle engineering costs of large-scale chemical 
projects optimization were optimized by setting constraints. 

2. Analysis of life cycle costs of large chemical project 
2.1 Overview of LCC analysis theory 

LCC analysis is an effective tool for analyzing investment decisions in engineering projects that was proposed 
in the cost management industry of Western countries in the 1980s (Swarr et al., 2011; Morris, 2010). LCC 
contains two basic points, namely the total costs that are directly related to products and consumed in the life 
cycle, and the correlation between LCC and the time value of funds. Also, the LCC analysis includes three 
main contents (Liang, 2014). First, determine the elements of the life cycle costs, and minimize the cost of 

                                

 
 

 

 
   

                                                  
DOI: 10.3303/CET1762245 

 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 

Please cite this article as: Yong Gu, 2017, Study on the life-cycle engineering cost management of large chemical projects, Chemical 
Engineering Transactions, 62, 1465-1470  DOI:10.3303/CET1762245   

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each element (Cleary et al., 2015). Second, associate life-cycle costs and system efficiency. Third, research 
the relationship between life-cycle costs and system efficiency (Emblemsvåg, 2003). 

2.2 Breakdown of life cycle costs of large-scale chemical projects 

The breakdown of the life cycle costs of a large-scale chemical project corresponds to the four phases of the 
project, namely the decision-making phase (Zhang, 2005), the implementation phase, the operations phase 
and the project closure phase (He and You, 2016). 
(1) Decision-making phase and implementation phase 
In the decision-making stage, the main construction contents and supporting facilities of the proposed 
chemical project are analyzed, such as raw material supply, process-oriented pipelines, equipment selection, 
environmental impact, and economic effect (Lenior and Verhoeven, 1990; Kohl and Wulke, 2004). As for the 
implementation stage, costs can be divided into design costs and construction costs. The design covers the 
total layout, process and technologies, and the overall design of various aspects, while the construction mainly 
refers to the construction based on the design drawings of all aspects, including manpower, materials, 
equipment loss, etc. (Peñamora et al., 1999; Bhimani, 1994). The cost compositions in the decision-making 
phase and the implementation phase are shown in Figure 1: 

 

Figure 1: The Cost Composition in the Project Decision Stage and Implementation Stage  

(2) Operations phase and project closure phase 
Operational costs mainly represent all costs incurred during the equipment operations in a chemical project, 
including costs for production, and equipment renewals and maintenance (White and Fortune, 2002; Ruiz-
Martin and Poza, 2015). And the costs in the project closure phase mainly refer to the costs generated in the 
refurbishment or demolition phase of major chemical equipment (Stevens, 1986; MehranSepehri, 2012). The 
costs in the operations phase and the project closure phase can be seen in Figure 2: 

 

Figure 2: The Cost Compositions in the Project Operating Stage and Closure Stage  

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2.3 Steps to analyze life-cycle costs of large-scale chemical projects  

According to the characteristics of large-scale chemical projects, life-cycle cost analysis can be divided into 
seven steps as follows (Yu et al., 2006; Chen, 2003). Firstly, determine the research target and identify the 
target requirements and performance parameters. Secondly, propose a number of feasible plans that meet the 
performance requirements of the project. Thirdly, establish a life-cycle costs estimation model (Ogihara et al., 
2003; Hollmann and Querns, 2003). Fourthly, collection data and information to make different assumptions 
about discount rates, inflation rates, economic lifetimes, etc. Fifthly, calculate the life-cycle costs of each plan. 
Sixthly, choose the optimal plan. Seventhly, give decision-making recommendations (Zakeri and Syri, 2015). 
Figure 3 displays the process of analysis of large-scale chemical projects’ life cycle costs. 

 

Figure 3: Large-scale Chemical Project Life Cycle Cost Analysis Process 

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3. Life cycle cost models of large-scale chemical projects  
3.1 Basic LCC Model 

The life cycle cost estimation methods for engineering projects have changed from the initial static estimation 
model into a dynamic estimation model with consideration of the time value (Zapalac et al., 1994). Despite 
different manifestations, models, in essence, all consider the project's initial construction fee, operating 
expenses, end-of-use disposal costs, and the time value of money (Ferchichi et al., 2015). The classic LCC 
estimation model is shown in Formula 1. 

LCCpv=K0+M0+i=1T(Kt+Mt+Et)(1+r)t-VT1+rT (1) 

In the formula, LCCpv is the total costs, and K0 and M0 refer to the investment cost and management cost of 
the chemical project in 0 year respectively. Kt and Mt are the investment cost and management cost of the 
project in the tth year respectively. Et means other costs in the he tth year, with VT as the residual value of the 
chemical project and T as the life of the project. 
In fact, due to the long investment cycle of large-scale chemical projects, both the internal and external 
investment environment in the project implementation stage are changing. At the same time, due to the impact 
of changes in raw materials, product demands, labor costs and investment environment on the costs of 
chemical projects, the accuracy of this model remains to be improved. 

3.2 All-factor LCC model of large-scale chemical projects 

Considering the time value of funds, the author introduced the idea of real options to correct the project value 
changes caused by the uncertainties such as the changes in the real value in the construction process. And 
based on the project’s risk cost, quality risk cost, safety risk cost, and environmental risk cost, the all-factor 
LCC model of large-scale chemical projects was obtained, as shown in Formula 2. 

LCCpv=t=0T1-1i=1nPit(1+r)-t+t=T1T1+T2-1i=1nCit1+r-t+t=T1+T2T1+T2+T3-1i=1nRit1+r-t+t 

=0T1+T2+T3-1i=1nQit1+r-t-i=1nVTi1+r-T1+T2+T3+ROs 
(2) 

In the formula, LCCpv denotes the total discounted value, and Pit, Cit, Rit, and Qitt represent the decision-
making and research costs, design and construction costs, operating cost, and the discounted value of factors 
of the device i in the tth year respectively. VTi refers to the end-of-use disposal residue value of the device i. 
T1, T2, and T3 respectively mean the decision-making and research time, design and construction time, and 
operations time. R represents the discount rate, and ROs represents the real option value of the chemical 
equipment. The above model involves the life cycle costs of chemical engineering projects at all stages, cost 
of influencing factors, real option value of the project, and the time value of funds for the above expenses, 
making it an open all-factor LCC model (Liu et al., 2012). 

3.3 Life-cycle engineering costs optimization for large chemical projects 

The optimization is to reduce the construction cost under the guidance of LCC theory by selecting the 
decision-making variables and establishing the optimization objective function and constraints. And then the 
global optimal costs is achieved by realizing local optimal costs at all stages of the life-cycle engineering costs 
of chemical projects. 
The main objectives of LCC optimization are multiple feasibility plans in the project decision-making phase. 
The optimization covers the construction scale, product solutions, raw material and fuel power supply 
solutions, process technology and equipment plans, utilities and supporting facilities solutions, environmental 
protection solutions, and operating costs and benefits in the operating stage. 
3.3.1 Constraints 
LCC optimization needs to meet the basic requirements of various technologies. P (x) is a function of the 
design scheme. YsX, YTX, YFX, YEVX, YENX, and YAX respectively represent the standard norms 
constraint, skills performance constraint, functional constraint, environmental constraint, energy consumption 
constraint, and aesthetic constraint, with all the constraints no more than P (x). 
3.3.2 Optimized model 
Bring the constraints into Formula (2) to obtain the optimized all-factor LCC model. As shown in Formula 3, 
the model can give the lowest life cycle engineering costs plan, a satisfactory result. 

LCCpv=i=0T1-1i=1npi=1pnkpiit(1+r)-t+t=T1T1+T2-1i=1n[ci-1cnYciit+ck-1clpckit×Lckit×1+ 

dckit+fit(h)(1+r)-t]+t=T1+T2T1+T2+T3-1i=1n[(rj=1rmmrjit+rk=1reerkit+rl=1rssrlit+rh=1rwwrhit)× 

(1+r)-t]+t=0T1+T2+T3i=1nQit(1+r)-t-i=1nRie×if=1igEif-Wic-Wi×1+r-T1+T2+T3+ROs 

(3) 

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=f(p)+f(c)+f(r)+f(q)-f(v)+f(s) 

In the formula, f(p) is the present value cost (PVC) function at the decision-making stage, with f(c) as the PVC 
function at the project implementation stage, f(r) as the PVC function at the operating stage, f(q) as the PVC 
function of factors influencing the project costs, f(v) as the present residual value function at the waste 
disposal phase, and f(s) as the present value function of the real option of the project. 
The mathematical optimized LCC model can be expressed as Formula (4): 

minLCCpv=W[ f(p)+f(c)+f(r)+f(q)-f(v)+f(s)] (4) 

Since it is extremely difficult to find the global optimal solution directly from the above formula, for specific 
projects, only a few major factors can be considered to establish a simplified mathematical model to find the 
local optimal solution to the costs. 

4. Conclusion 
In order to optimize the management of life-cycle engineering costs of large-scale chemical projects and 
optimize the investment decisions in chemical projects, this paper conducted relevant studies by following the 
LCC theory. The main innovations are as follows: 
(1) The structure of life cycle costs of large-scale chemical projects has been identified, as well as cost 
analysis steps. 
(2) In line with the basic LCC model, an all-factor LCC model for large-scale chemical projects has been built 
by taking the factors such as quality, safety and environment into consideration. Additionally, the model has 
been optimized based on the constraints, leading to the optimized all-factor LCC model for the investment 
decision-making in large-scale chemical engineering projects. 

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