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Designing a Surrogate Fuel for Gas-to-Liquid (GTL) Derived Diesel Hanif Ahmed Choudhury, Saad Intikhab, Sawitree Kalakul, Muzammiluddin Khan, Reza Tafreshi, Rafiqul Gani, and Nimir O Elbashir Energy Fuels, Just Accepted Manuscript • DOI: 10.1021/acs.energyfuels.7b00274 • Publication Date (Web): 14 Aug 2017 Downloaded from http://pubs.acs.org on August 19, 2017
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Modeling
Combustion
GTL Diesel
Physicochemical property
Density Viscosity Flash Point Distillation ……………..
Diesel
GTL Diesel
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Designing a Surrogate Fuel for Gas-to-Liquid (GTL) Derived Diesel
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H.A. Choudhurya, S. Intikhaba, S. Kalakulb, M. Khanc, R. TafreshiC, R. Ganib and N.O. Elbashira,d
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a
b
Chemical Engineering Program, Texas A&M University at Qatar, 23874 Doha, Qatar Department of Chemical and Biochemical Engineering Program, Technical University of Denmark, DK-2800 Lyngby, Denmark a Mechanical Engineering Program, Texas A&M University at Qatar, 23874 Doha, Qatar d
Petroleum Engineering Program, Texas A&M University at Qatar, 23874 Doha, Qatar
Keywords: GTL diesel, surrogate, fuel properties, combustion, emission
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Abstract: Synthetic diesel fuel produced from natural gas via the Gas to Liquid (GTL) technology is referred to as ultra-clean fuel but still challenged for full certification as diesel fuel. GTL diesel lacks certain hydrocarbons and chemical constituents, which although are benign to environment, result in a trade-off in performance when used in a diesel engine. To boost GTL diesel physicochemical properties and thereby enable its use in conventional diesel engines, GTL diesel needs improvement. This can be achieved by mixing suitable additives to the GTL diesel and through the development of surrogate fuels that have fewer components. Screening of thousands of additives is a tedious task and can be done efficiently via computer based modeling to quickly and reliably identify a small number of promising candidates. These models are used to guide the formulation of five surrogates and predict their physicochemical properties. These surrogates are further verified using rigorous mathematical tools as well as through advanced experimental techniques. An optimal surrogate MI-5 is identified, which closely mimics a GTL diesel-conventional diesel blends in terms of its physicochemical properties. An engine study for the surrogate is also performed to understand the effect of physicochemical properties on combustion as well as emission behavior of the fuel. MI-5 exhibited an optimal torque at higher load conditions. A reduction of 11.26% NOx emission for MI-5 is observed when compared to conventional fuel. At higher loads, diesel fuel surpasses the total hydrocarbon (THC) emissions for both the surrogate and the GTL fuel. No significant variation in CO and CO2 emissions for MI-5, GTL diesel and conventional diesel are observed. Analysis of combustion as well as emission behavior of the fuels helps to understand the role of physicochemical properties on the performance of the fuel.
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1. Introduction
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Gas-to-Liquid (GTL) fuels derived from the Fischer-Tropsch synthetic process have gained increased
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attention due to their significant supply coming from major plants such as the Pearl GTL plant in
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Qatar1. The focus on GTL fuels is mainly driven by the need to reduce emissions of greenhouse gas
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(GHG) and their ability to complement dwindling world fuel supplies
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environmentally benign (due to the lack of aromatics and sulfur), GTL fuels fall short of meeting
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critical physical properties that affect fuel combustion behavior, as opposed to conventional crude oil
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based fuels. For example, pure GTL diesel when tested in an unmodified engine control unit of a test
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engine, exhibited slightly lower torque, power and brake thermal efficiency (BTE) due to lower density
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and bulk modulus of the GTL diesel4. Therefore, GTL fuels are typically blended with crude oil-based
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conventional fuels to be used in conventional compression ignition (CI) engines5. At present there are
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no established specifications for blending GTL diesel with conventional diesel as in the case of
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synthetic paraffinic kerosene (SPK) blends (ASTM 7566/1655), wherein an upper limit of 50 (vol%) of
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SPK is permitted in conventional jet fuel. Therefore, it is contingent on refineries to dictate the blend
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ratios. Typically, GTL fuels mostly comprise n- and iso-paraffinic compounds. However, when GTL
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diesel is blended with conventional diesel, it yields a complex blend that consists of aromatic and cyclo-
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compounds in addition to n- and iso- alkanes. Formulating such complex blends consisting of hundreds
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of individual compounds via computer aided modeling naturally poses a tremendous optimization
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challenge. Such techniques require details of each compound, chemical kinetic rate constants and
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thermodynamic property model parameters, all of which are currently not available 6. Moreover, testing
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of these blends will require excessive amount of time and resources.
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A feasible alternative is to employ a ‘surrogate’ fuel that represents a GTL diesel-blended conventional
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diesel. A surrogate is a mixture of a smaller number of chemical compounds with known compositions
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and properties. Dooley et al.7,8 reported development of a four component surrogate for jet fuel to
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emulate the gas phase combustion kinetics of their fuel. They provided a comprehensive data set of
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combustion kinetics to aid numerical modeling of combustion process of similar complex fuels. They
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proposed the conceptual theory of fuel oxidation and used it to provide a methodology for the
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formulation of surrogates.
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Shrestha et al.9 reported the development of six different surrogates using a MATLAB program to
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emulate the ignition delay and rate of heat release of the JP-8 surrogate for diesel engine application.
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They developed a MATLAB code to identify surrogate components that closely match the target fuel.
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More recently, Kang et al.10 performed combustion as well as experimental validation studies on Jet-A
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surrogates developed via a model-based optimizer. Their experimental validation study revealed that
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surrogates developed using a model-based optimizer show acceptable agreement with the target Jet-A. 1 ACS Paragon Plus Environment
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. Despite being
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Pitz and Mueller
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and discussed the experimental and modeling work on some critical diesel surrogate compounds. Prak
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et al. 6 studied the chemical composition and physical properties of algal-based hydro treated renewable
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diesel (HRD) to develop a surrogate mixture. They tested the surrogate in a Yanmar engine along with
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HRD fuel to compare and evaluate the engine performance in terms of start of ignition, ignition delay,
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overall combustion duration and maximum rate of heat release 6. Mueller et al.
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four ultra-low sulfur diesel surrogate mixtures to be investigated in CI engine and combustion vessel
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experiments.
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Although there have been numerous reports on surrogate development for conventional diesel fuel and
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Jet fuel to understand their behavior during combustion, no similar attempt was made to develop a
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surrogate for GTL blended diesel fuel. The goal of this study is to develop a surrogate that can represent
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a typical blend of GTL diesel and conventional diesel. Such a blend can therefore be used as a baseline
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for future studies aiming to improve the performance of GTL diesel either via blending of conventional
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diesel or via mixing of additives to the pure GTL diesel. Therefore, an attempt is made in this paper to
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formulate a representative GTL diesel-conventional diesel blend surrogate whose physio-chemical
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properties are tailored through a non-empirical Equation of State based (EOS) model. The purpose of
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this study is to gain insight into the effect of the surrogate’s physicochemical properties on its
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combustion as well as emission behavior. For the sake of simplicity, the “GTL diesel-conventional
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diesel blend surrogate” will be referred to as “surrogate” throughout this paper. The data presented
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herein will help enable combustion modeling of real fuel and characterization of surrogate's combustion
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behavior in the engine will give the insight to understand their capabilities/limitations to represent the
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targeted fuel. The paper is organized as follows: Section 2 discusses surrogate fuel design and
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experimental testing methodologies; Section 3 describes an approach to experimentally verify the
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model predictability of the fuels' physical properties as well as the role of the chemical compounds
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present in the surrogate on the fuel’s physicochemical properties. Section 3, also includes engine
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performance tests based on combustion and emission behavior for the surrogate diesel, GTL diesel, and
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conventional fuel. The last part of this paper is the conclusion and recommendation for future work.
have reviewed the progress in the area of surrogates for conventional diesel fuels
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formulated a set of
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2. Materials and methods
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Yunus et al.2 reported a systematic methodology to design tailor-made blended products using a
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computer-aided technique. They developed three supporting tools; a chemical database, a property
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model library and a blend composition optimizer associated with their methodology. Further, they
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applied their methodology to case studies involving the design of gasoline and lubricant blends as a
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validation of their technique.
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A similar methodology has been adopted-applied in this work to formulate five surrogates that represent
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a GTL diesel-conventional diesel blend to understand the role of chemical compounds in the blend and
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then to fine-tune the physicochemical properties that affect the combustion behavior of the surrogate
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fuel. Various compositions are proposed via this adopted technique and changes in the final
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compositions of the surrogates are fine-tuned in conjunction with the experimental feedback. The
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experimental campaign consists of preparing different surrogates and measuring important properties
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that have been predicted by the model-based technique, such as, density (ρ), kinematic viscosity (ν),
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vapor pressure (VP), flash point (Tf) and high heating value (HHV). Other properties that were not
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constrained in modeling, such as, cloud point (CP), pour point (PP), distillation profile, and calculated
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Cetane index (CCI) that are critical for a diesel fuel have also been measured and compared with
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conventional diesel and pure GTL diesel. The last step of the investigation involved a preliminary
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engine test with the surrogate to investigate its capability to be run on an un-modified set-up and to
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ascertain compatibility with the conventional diesel and GTL diesel. A more comprehensive
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combustion study will be undertaken to investigate the effect of physicochemical properties on
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combustion and emission behavior of the fuel in detail. Following topics are included in this section: (i)
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brief description of the algorithm and the models used to design the blends representing the surrogates,
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(ii) list of chemical compounds, blending techniques and blend verification methods, (iii) experimental
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techniques to measure the physicochemical properties of the blends, and (iv) methods used for the
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combustion and emission study.
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2.1.
Diesel target properties and calculation models
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The surrogates investigated in this study were formulated in-silico via the workflow shown in Figure 1.
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The objective of step 1, termed ‘problem definition’, is to identify the product needs and translate them
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into physicochemical properties with target values that need to be matched. This step requires prior
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knowledge coming from a thorough understanding of the material physics, thermodynamics, reaction
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kinetics and chemistry related to the use of the product (in this case, diesel), as well as knowledge from
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peer-reviewed articles and other information databases. As Yunus et al.2 pointed out, there is clearly a
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need to develop a reliable knowledge base with information from relevant publications, patents etc.,
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which has been developed for design of tailor-made diesel. The new formulated surrogate should have
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good fuel performance and meet or exceed stringent requirements for worldwide fuel handling and 3 ACS Paragon Plus Environment
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product standards as listed in Table 1. The objective of step 2 is to formulate the tailor-made diesel
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blend design as a mathematical optimization problem, the Mixed Integer Non-Linear Programming
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(MINLP) problem, using molecular, structural, mixture, target-property and process constraints. , as
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presented as Eq. (1) – (3). The linear target property constraints are: HHV, ρ and -logLC50 (Eq. 2), while
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the non-linear constraints are: RVP, flash point temperature (Tf) and kinematic viscosity (Eq. 3). The
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property model equation details are given in Appendix.
7 ( )
(1)
≤ ≤
(2)
(, ) ≤
(3)
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where is molar fraction of compound i in the mixture; is the pure component property j of
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compound i; is non-linear property K; X is a vector of compositions; D is a vector of model
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parameters; UB is a upper bound value of the linear property; LB is a lower bound value of the linear
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property; Details of the model may be found in Yunus et al2 and Gani et al13. In step 3, a solution to the
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above MINLP problem is achieved14 via strategies such as: database search; generate-test approach
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(first generate candidates that satisfy the constraints and then order the feasible candidates in terms of
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their objective function values); simultaneous solution approach (use an appropriate optimization
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algorithm to solve the MINLP problem); and decomposition approach (decompose the main problem
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into sub-problems and solve these sub-problems according to a predefined solution order). The
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computer-aided tools used in this step are highlighted in Figure 1. Finally, in step 4, a small number of
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promising candidates from step 3 are selected for experimental verification and fine-tuning either
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through rigorous computational model-based tests or experimental tests as suggested by the Design of
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Experiment toolbox. In this step, the stability of the product, the desired performance, the target
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properties, the color, etc., are verified. Note that with the above problem formulation, while the final
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selected surrogate will have a single final value, use of bounds on the target properties provides a more
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flexible solution approach. This is because for a single target value, a fixed target value can be matched.
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However, for more than one target property, it may not be possible to match all the fixed values of the
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target properties. Thus, bounds help to find candidates from which the most appropriate can be selected.
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Figure 1.
1 2 3
Table 1.
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In this study five surrogates (namely MI-1 to MI-5) were formulated as described above. Their
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compositions are given in Tables.
Table 2
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2.2.
Chemical compounds’ procurement, handling and blending
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All the chemicals used to prepare the surrogate fuels are listed in Table 3. A GTL diesel fuel and the
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conventional diesel fuel are obtained from local venders.
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Table 3
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Approximately 500 ml. of each surrogate fuels are prepared by adding a desired volume of the chemical
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compound to a container using different cleaned pipettes for each compound. The ASTM D5854
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method is followed for preparing these blends. The prepared surrogate fuels are shaken vigorously for
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about one minute to ensure proper mixing.
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2.3.
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For the all the blends along with GTL diesel and conventional diesel, the following physical properties
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are determined using different equipment and standards.
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•
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•
•
•
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Flash point, Tf is measured using Pensky-Martens Closed Cup Flash Point Tester (PM 93) by Stanhope-Seta according to ASTM D93.
•
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Cold flow properties analyzer by Phase Technologies is used to measure cloud point, CP and Pour point, PP according to ASTM D5773 and ASTM D5972, respectively.
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Kinematic viscosity, ν is measured using Stabinger viscometer by Anton Paar according to ASTM 7042.
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Density, ρ is measured using a density meter (DMA 4100) by manufacturer Anton Paar according to ASTM D4052.
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Properties testing methods
Vapor pressure, VP for the blends is measured using Equipment MiniVapXpert by manufacturer Grabner instrument according to ASTM D6378.
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High heating value, HHV is measured using the bomb calorimeter by Parr Instrument according to ASTM D240. 5 ACS Paragon Plus Environment
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Distillation Curve is determined according to ASTM D86 using a Distillation Unit by Petrotest
•
2 3
Company. Cetane number, CN is calculated using ASTM D4737, which uses a correlation that has been
•
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established between the ASTM CN and the density and 10%, 50% and 90% distillation recovery
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temperatures of the fuel. This test method (D4737) is a supplementary tool for estimating Cetane
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number when it is not possible to obtain result from ASTM D613. In this article, the CN is thus
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described as Calculated Cetane Index (CCI). Please note that this test method is not a routine
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method for measuring ASTM Cetane number; for verification, experimental measurement has to be
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performed using ASTM D613.
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2.4.
Combustion and emission study
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The combustion study is performed in an air-cooled Yanmar Direct Injection LV100 series single
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cylinder diesel engine. The key purpose of the experiment is to analyze and perform a detailed engine
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performance and emission characteristic study using the three different fuels: conventional diesel, GTL
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diesel and a surrogate. No modifications are made to the engine in any way for testing the different
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fuels. The specifications of the engine are given in Table 4.
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Table 4
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A hydraulic brake dynamometer is also utilized for the purposes of this experiment. The dynamometer
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is operated in remote mode for all runs after the input of similar drive cycles for all fuels. The load
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acting on the engine is increased or decreased via a hydraulic regulator. The RPM is maintained
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constant via an in-built controller, which augments the throttle that in turn controls the input of fuel. A
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load cell attached to the output shaft of the engine measures the resulting torque produced by the
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engine. The sampling rates for both engine RPM and net resultant torque output are both set to 1 Hz.
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Two specific runs at different RPMs are performed namely, 1500 and 2500 RPM, respectively. The
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total run-time is 7 mins with load ranges varying from 5% to 100% being applied under identical step-
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wise incremental conditions for all preceding engine RPMs. The central computer console then records
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the different parameter values, such as, net torque (Nm), engine speed (RPM) and exhaust temperature
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Tex (°C), via thermocouples placed in the exhaust manifold.
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The engine is run for a statutory period of 5 min after the change of the fuel to ensure all fuel lines and
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internal components of the engine have been saturated with the new fuel and to rule out any
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discrepancies in the data obtained. The exhaust from the engine is sent to a pre-filtering element to help
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remove the particulate matter (PM) and generated soot. The gases are then sent to the Horiba MEXA
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7170 DEGR analytical emissions testing bench via heated sampling lines. The sampling rate for the
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emissions study is also set to 1 Hz. The total hydrocarbon (THC) concentrations are measured by the 6 ACS Paragon Plus Environment
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principle of flame ionization detector (FID); CO and CO2 concentrations are measured via a non-
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dispersive infra-red (NDIR) analyzers. NOx and its derivatives are measured via chemiluminescent
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analyzers.
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3. Results and discussion
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The results are presented and discussed in the following order: the first part covers the model
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predictability of the critical properties for five surrogate blends using advanced experimental setup as
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well as the distillation profiles of our fuels in sections 3.1, 3.2 and 3.3; the second part discusses the
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correlation between the physicochemical properties of the surrogates and their hydrocarbon
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composition (section 3.4); and finally investigating the role of the physical properties on engine
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performance via combustion and emission studies (sections 3.5 and 3.6).
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3.1.
Composition of surrogate mixtures
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Compositions of five surrogates are given in the Table 2. The first developed surrogate (MI-1) was
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designed to represent, as closely as possible, typical GTL diesel, to act as a reference fuel. The second
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surrogate (MI-2) is formulated to ensure it comprises iso-, cyclo- and aromatic compounds to closely
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represent GTL diesel blended with conventional diesel. However, 2, 2, 4-trimethylpentane,
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commercially known as iso-octane, present in the MI-2, has very low Tf ( −12 οC), which affects the
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overall blend’s Tf . It is essential to have a high Tf value for the diesel fuel (>38 οC) since it determines
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the safe handling of the fuel. As a result, the third surrogate (MI-3) was designed replacing iso-octane
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with iso-cetane (Tf : 96 οC). It is to be noted that aromatic concentration in surrogates MI-2 and MI-3
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was optimally predicted by the model to be 20 vol%, which is significantly higher than that of a typical
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GTL-blended diesel fuel. Aromatics have an inverse effect on the emission profile of any fuel as their
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presence in high concentrations will lead to incomplete combustion15. Therefore, a lesser concentration
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is always desired to control the emission of fuel during its combustion. Additionally, Tetralin, used to
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serve as the aromatic part in surrogates MI-2 and MI-3, is a cause for concern as it may produce
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explosive peroxides on combustion as evident from the Safety Data Sheet provided by the supplier. It is
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noted, there are a few reports in the open literature where combustion studies were performed with
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Tetralin11,12,16–25, . In this study, a more conservative approach is followed and decision was made to (i)
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lessen aromatic concentrations and, (ii) use a safer molecule than Tetralin.
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Therefore, Tetralin was substituted with Toluene in MI-4. Since the deviation of predicted versus
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experimental values of MI-4’s Tf and VP of MI-4 was found to be high, and additional additive was
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recommended. As a result, in MI-5, n-Decane was added, which significantly improved RSD values 7 ACS Paragon Plus Environment
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(Table 5). MI-5 comprises all the hydrocarbon building blocks similar to that of a GTL diesel-
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conventional diesel blended fuel and can be regarded as an ‘optimal’ candidates for a surrogate.
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Table 5
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3.2.
Model prediction versus experimental measurements
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To verify the model predictions on the physicochemical properties, the five surrogates are tested in the
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Fuel Characterization Lab utilizing advanced analytical instruments. The experimental results of the
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targeted properties (ρ, ν, VP, Tf and HHV) are measured and compared to the model predicted values as
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given in Table 5. The variations between the model prediction and experimental results are expressed in
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terms of the Relative Standard Deviation (RSD). RSD is defined as the ratio of standard deviation (σ)
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and mean (µ) and is expressed as a percentage as shown in Eq. (4).
14
= /! × 100 (4)
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Model predictions for MI-1 are found to be in close agreement with experimental results for all the
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target properties viz. ρ, ν, VP, Tf and HHV as evident from their RSD values of 0.06%, 0.19%, 6.59%,
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0.32% and 1.15%, respectively. Whereas, for MI-2, MI-3 and MI-5, small RSD values are observed for
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only the following target properties: ρ, Tf and HHV as given in Table 5. It is worth noting that both ρ
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and HHV values predicted by the model are in good agreement with experimental results for all
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surrogates, which implies that the linear mixing rule assumption for calculating ρ and HHV for these
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blends is appropriate. Elmalik et al 1 has also observed a linear trend with respect to constituent’s mass
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fraction for ρ and HHV.
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However, in the case of MI-4 the ν, VP and Tf are found to be in poor agreement with the experimental
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results as evident from their large RSD values of 11.36%, 67.39% and 28.34%, respectively. MI-4
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comprises approximately 45(vol%) of n-paraffinic compound in contrast to all other blends which
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comprises ≥55(vol%). The greater volume of the other hydrocarbon classes (iso- and cyclo-) present in
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MI-4 produces greater intermolecular interactions. This in turn renders a non-linearity in the target
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properties of MI-4 that leads to this observed deviation in model predictions from experimental data.
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The non-linearity is accounted for in revised calculations for MI-4 with models available in Virtual
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Product-Process Design Lab (VPPD-lab)26. The new results of ν, VP and Tf are given in Table 6,
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clearly shows an improvement in the RSD values.
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Table 6
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3.3.
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The distillation profile is not used here as a fitting criterion but rather to validate the formulated
7
surrogates against conventional diesel and GTL diesel fuels. Figure 2 shows the comparison of
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distillation profiles of surrogates with pure GTL diesel and conventional diesel. Front end of the profile
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(10 vol%) helps determining: (1) easing hot starting, (2) easing cold starting, (3) avoiding vapor lock,
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and (4) lowering evaporation and running-loss emissions. Midrange of the profile (50 vol%) helps
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determining:(1) fast warm-up and smooth running, (2) superior short-trip fuel economy, (3) good
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acceleration and power, and (4) defense against carburetor icing and hot-stalling. Tail-end of the profile
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(90 vol%) helps determining: (1) superior fuel economy after engine gets warmed up, (2) no engine
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deposits, (3) minimal fuel dilution of crankcase oil, and (4) minimal volatile organic compound (VOC)
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exhaust emissions.
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MI-1 and MI-3 have a slightly higher initial boiling point (IBP) than that of GTL diesel. The IBP of MI-
17
1 and MI-3 indicates that these two fuels will have easy hot and cold starting. All the surrogates except
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MI-1 have poor match with the middle and tail end of the distillation profile of GTL diesel. This
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shortcoming can be attributed to the shorter carbon chain length compounds present in all the surrogate
20
blends except MI-1 which also comprises of C18 and C20 compounds. Pitz and Mueller
21
review also suggested that compounds, which lie in the carbon range (C10-C22) are more
22
representative of diesel fuel. It has been noted by Won et al.27 that the use of component that have a
23
molecular weight near the average for the real fuel would be beneficial to better match the distillation
24
property of the target fuel. The average molecular chain lengths of all the surrogate blends are given in
25
Table 7, and calculated by the method described in Jeng28. In the present study, it is observed that MI-1,
26
which has an average chain length of 14.5, shows an excellent match with the distillation profile of
27
GTL diesel. Whereas, all the other surrogate fuels (MI-2, MI-3 and MI-5) have a much lower average
28
chain length of approximately around carbon 11, which could be the reason behind a poor match with
29
the distillation profile of either GTL diesel or conventional diesel. Therefore, use of longer chain
30
compounds (C15-C16) in the blends will enable a better matching of the distillation profile of any
31
surrogate fuel with the GTL fuel.
32
Distillation Profile
Table 7
33 9 ACS Paragon Plus Environment
11
in their
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Energy & Fuels
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MI-2, MI-3 and MI-5 are more volatile as compared to MI-1 and therefore, the distillation profiles are
2
also towards much lower temperatures that infers an improved atomization and dispersion of fuel spray.
3
It may also lead to a more combustible air-fuel mixture as lower distillation characteristics ensure ease
4
of evaporation. Moreover, reduced smoke and Particulate Matter (PM) emissions are also expected for
5
these more volatile surrogates. It is worth mentioning that the scope of this work is not to compare the
6
results with ASTM specifications, however the distillation profile of MI-2, MI-3 and MI-5 comply with
7
Grade 1 and MI-1 and GTL diesel complies with Grade 2 of ASTM D975 specifications.
8
Figure 2
9 10
3.4.
Correlation between physicochemical properties
11
In this section comparisons of physicochemical properties of tested fuels are done to investigate the
12
role of constituent chemical compounds on individual fuel physicochemical properties. Each target
13
physicochemical property is contrasted with the one that could possibly influence the other.
14
3.4.1. Density (ρ) and kinematic viscosity (ν)
15
Figure 3 shows a comparison of ρ and ν of the surrogates with pure GTL diesel and conventional diesel.
16
MI-1 consists entirely of n-paraffinic compounds and is comparable with pure GTL diesel which is
17
highly paraffinic in nature. The lower ρ values for MI-1 and pure GTL diesel can be attributed to the
18
lack aromatics 1. The effect of aromatics on ρ is observed by increasing its concentration from MI-5