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Production and sustainability aspects of biodiesel (fatty acid methyl esters, FAME) or potential feedstocks are studied in the IEA-AMF Task 45 (Stengel and Vium 2015), Task 37 (Nylund and Koponen Eds. 2012) Task 34-1 (McGill et al. 2008) and Task 30 (Greene and Dawson Eds. 2007). Use of biodiesel as a substitute diesel fuel is on the rise around the world. Volumes of biodiesel used and produced are growing very rapidly from nearly zero in just the mid-1990s to over 10 Mtoe in 2009 (AMF Annual report 2010). In 2015, global production of biodiesel was already 23.5 Mtoe (30.1 billion liters), which represents 22% of global biofuels production, while share of ethanol production was 74% (50 Mtoe, 98 billion liters) and of HVO production 4%, respectively (REN21 2016).


Such a rosy outlook for biofuels is not without technical hurdles, though. Esters from vegetable oils face some serious technical barriers that either require special measures to accommodate the fuels or limit their practical use in some climates at some blend levels. Among these barriers are poor oxidative stability, incompatibility with some elastomers, low-temperature flow properties, high NOx emissions, and competition for the same resources that are used in the food industries. If we are to achieve greater impact of bio-derived fuels, we must utilize all varieties of biomass feedstocks and produce a broader slate of fuel choices, ranging from gasoline replacements to diesel replacements. Therefore, the world’s attention is turning to concepts of more diverse manufacturing processes, and the notion of a flexible biorefinery is coming into being. Amongst these are paraffinic fuel options (HVO) (IEA-AMF Task 34-1: McGill et al. 2008).


Ignition properties of FAME biodiesel are acceptable with cetane numbers generally over 50. FAME contains practically no sulfur or aromatics, and lubricity is good. Drawbacks are related to high viscosity, poor cold properties, high boiling point and impurities, such as triglycerides, glycerol, alcohols, sodium, potassium and phosphorus (Graboski et al. 1998, WWFC 2006,

Chemical structure

Vegetable oils, animal fats, recycled cooking greases etc. can be transformed into biodiesel using transesterification (Figure 2). Oils and fats, which are triglycerides and/or free fatty acids react with alcohol to produce esters when using catalyst, which is typically sodium or potassium hydroxide. The side-product is glycerol (glycerine). So far, only methanol is used as alcohol in current biodiesel plants. Although also other alcohols have been studied, for example, by Lang et al. (2001) and Knothe et al. (1997). Processes and catalysts used today are optimized for methanol. Yields tend to be lower for higher alcohols than for methanol. Cetane number may increase with higher alcohols, as well as viscosity. In this section, only fatty acid methyl esters (FAME) are discussed. 

Figure 2. Schematic process of transesterification of fatty acids with methanol to methyl esters and glycerol.
R = carbon chain of fatty acid.

Biodiesel esters can be made from a variety of vegetable oils and fats, including those presented in Table 1.

Table 1: Feedstocks for biodiesel esters  (IEA AMF Task 34-1 McGill et al.2008).

Animal Fats Vegetable Oils Recycled Greases
Edible tallow Soy Used cooking oils
Inedible tallow Corn Restaurant frying oils
Lard Canola (Rapeseed)  
Yellow grease Sunflower  
Poultry fats Cottonseed  
Fish oil    

The oils and fats above are made up of 10 common types of fatty acids. All have between 12 and 22 carbon atoms with the great majority of them being between 16 and 22 carbons. Some are fully saturated, some monounsaturated (one double bond in the fatty acid chain), and some polyunsaturated (multiple double bonds in the fatty acid chain). The different feedstocks listed above are made up of different proportions of saturated, monounsaturated, and polyunsaturated fatty acids. This is illustrated in Figure 3. (IEA-AMF Task 34-1 McGill et al. 2008).

Figure 3. Compositions of types of fatty acids in various biodiesel feedstocks (NREL 2006).

The different levels of saturation of the feedstock can affect the properties of the finished biodiesel fuel. This proves to be a significant factor when selecting the best feedstock for the particular application planned for the finished biodiesel fuel. This fact is illustrated in Table 1 below. In the table, general trends in three fuel properties, cetane number, cloud point, and stability, are shown to be related to the degree of saturation of the feedstock. Shown are typical fatty acids of different carbon content and different levels of saturation. The fuels from saturated fatty acids are generally better performing in cetane number and stability, and as the number of double bonds increase, performance in those properties generally degrades. (IEA-AMF Task 34-1 McGill et al. 2008).

The selection of feedstock has general effects on the product of the esterification process, i.e. biofuels. On the other hand, fuel properties, physical, as well as, chemical, affect the performance of engines, e.g. on engine cleanliness and deposit build-up. For the diesel engine, fuel parameters like ignition quality (cetane), density, boiling range, content of aromatic compounds and sulfur affect engine performance and emissions. Properties like viscosity, lubricity, and the content of impurities may be decisive for engine durability, and these properties can vary by region depending on the weather of the region.(IEA-AMF Task 34-1: McGill et al. 2008).

Table 2. Variation of finished biofuel properties with feedstock composition (NREL, 2006)



12:0, 14:0, 16:0, 18:0, 20:0, 22:0


16:1, 18:1, 20:1, 22:1


18:2, 18:3

Cetane number High Medium Low
Cloud Point High Medium Low
Stability High Medium Low

Legislation and standards

In order to assure that certain minimum requirements are met by the fuel, international standards exist for biodiesel fuels. The standards ensure that important factors in the fuel production process are satisfied. These include low sulfur content and absence of glycerin, alcohol, catalyst, and free fatty acids. Basic industrial tests to determine whether the products conform to standards are specified in the standards rules.

The international standard for 100% FAME biodiesel in Europe is EN 14214, while ASTM D6751 is referenced in the U.S. and Canada. ASTM D6751 for neat biodiesel (B100) prior to blending, includes a voluntary No. 1-B grade, which provides more stringent controls for minor components in raw materials used to make biodiesel than the No. 2-B grade. The finished blended fuel standards are D975 for on/off road diesel up to 5% biodiesel (B5), D7467 for B6-B20 on/off road applications, and D396 for heating oil up to 5% biodiesel. B100 used for D975, D7467, and D396 must meet D6751 (either the No. 1-B or the No. 2-B grade) prior to blending. More information can be found at ASTM.ORG or NBB.ORG. (IEA-AMF Task 34-1: McGill et al. 2008).

In Europe, EN 14214 describes the requirements and test methods for FAME before blending with diesel, and  the several standards specify the requirements for fuels containing FAME:

  • EN 14214 (2013 + A2:2019): 100% FAME biodiesel
  • EN 590 (2014): for diesel fuel containing FAME up to 7% (%V/V)
  • EN 16734 (2016) specifies B10 fuel with FAME content up to 10 %(V/V) for compatible vehicles
  • EN 16709 (2015) specifies B20 and B30 fuels with FAME content from 14 to 20 %(m/m) for B20 and FAME content from 24 to 30 %(m/m) for B30 in fleet use

In Japan, diesel fuel specification JIS K 2204:2007 allows FAME content up to 5 %(m/m).

Automobile and engine manufacturers have defined recommendations for fuels in “World Wide Fuel Charter” (WWFC). Biodiesel guidelines for 100% FAME biodiesel came available from WWFC in 2009.

WWFC and two standards standards together with typical properties of RME are shown in Table 2.

Table 3. Example of FAME properties (Rapeseed Methyl Ester, RME) together with the requirements in the standards for 100% FAME. Complete requirements and standards are available from the respective organizations.


RME examplea

WWFC: 2009

Standard A

Standard B


C19 H342




Molecular weight, g/mol





Carbon/Hydrogen/Oxygen,  wt-%





FAME content, %(m/m)





Cetane number

min. 51a




Density at 15 °C, kg/dm3



0.860 -  0.900


Viscosity at +40 °C, mm2/s


2.0 - 5.0

3.5 -  5.0

1.9 -  6.0

Cloud point, °C

0 -  -5a


several grades





several grades







Initial boiling point, °C





Final boiling point, °C





Evaporated 90 vol-%, °C





Aromatics, total, %m/m





Polyaromatics, %m/m





Sulfur content, mg/kg





LHV heating value, MJ/kg

36a,  38b




LHV heating value, MJ/l

32a,  34b




Flash point, °C





Carbon residue on 10%

distillation, %m/m





Carbon residue on 100%

sample, %m/m





Ash content, %m/m





Sulfated ash, %m/m





Water content, mg/kg





Total contamination, mg/kg





Copper corrosion



Class 1

<No. 3

Ferrous corrosion at 50 °C


max. light rusting



Oxidation stability, 110 C, h





Cold soak filtration, s

- at temp. below -12°C





Acid number, mg KOH/g





Iodine value, g iodine/100 g





Linolenic acid methyl ester,






Polyunsaturated (>4 double bonds) methyl esters, %m/m





Methanol content, %m/m





Monoglyceride content, %m/m





Diglyceride content, %m/m





Triglyceride content, %m/m





Free glycerol, %m/m





Total glycerol, %m/m





Group I metals (Na+K), mg/kg





Group II metals (Ca+Mg), mg/kg





Phosphorus content, mg/kg





Water content, %m/m





* Or flash point 130 °C minimum
a Murtonen et al. 2009  b Rantanen et al. 2005  c Deutz Technical Circular 2016


Density and energy content

Energy density (energy per unit of volume) is the most basic of fuel properties, and it is one of the largest determinants of fuel economy, torque, and power delivered by the fuel. The energy content of petroleum diesel fuels can vary up to 15% between suppliers or between seasons of the year due to different refining parameters. Number 2 diesel (U.S.) usually has larger energy density than Number 1 diesel, and summer grade larger than winter grade. When compared to petrol-diesel the process of making the biodiesel (B100 if not blended with diesel fuel) has less effect on the energy density than the choice of feedstock. This results from the fact that the feedstocks for biodiesel do not vary as much as the crude oil does when making diesel fuel. Biodiesel as an oxygen-containing fuel (about 11% by weight), generally has lower heat content than petrol-diesel, and this results in lower power, torque, and fuel economy for B100. Figure 4 shows a comparison of biodiesel heating values for various feedstocks compared with petrol-diesel. (IEA-AMF Task 34-1: McGill et al. 2008).

Figure 4. Lower heating value (LHV) for diesel fuel and biodiesel fuels (B100) (National Renewable Energy Laboratory, NREL 2006).

Cold properties

Cold properties of the fuel can have significant impact on whether the fuel, petroleum-derived or bioderived, can be used reliably in certain geographic areas and in the cold seasons of the year. Both petrol-diesel and biodiesel can freeze or gel at cold temperatures and, as a result, clog filters or become too viscous to pump thus disabling a vehicle. Cold flow properties of fuels are described with three different measures, namely cloud point, Cold filter plug point, and Pour point. It should be noted that the standardized test methods have been developed for petroleum products, and do not necessarily depict the true performance of various biofuels.

The cloud point for B100 is around 0 °C for most vegetable oil-derived biodiesel fuels, but it can go as high as 27 °C for biodiesels from animal fats and frying oils. Table 3 below shows the cold flow properties for various B100 biodiesel fuels made from different feedstocks. Note that there is not a great difference in temperatures between the cloud point and the pour point, which suggests that when the freezing process begins, it proceeds quickly to the point where the fuel is unusable. The cold flow properties of biodiesel can be improved with special additives, or by blending it with winter grade diesel fuel. (IEA-AMF Task 34-1: McGill et al. 2008).

Table 4. Cold flow properties for various B100 fuels (NREL 2006).

Test Method Cloud Point
ASTM D2500
Pour Point
Cold Filter Plug Point
IP 309
B100 Fuel °F °C °F °C °F °C
Soy Methyl Ester 38 3 25 -4 28 -2
Canola Methyl Ester 26 -3 25 -4 24 -4
Lard Methyl Ester 56 13 55 13 52 11
Edible Tallow Methyl Ester 66 19 60 16 58 14
Inedible Tallow Methyl Ester 61 16 59 15 50 10
Yellow Grease 1 Methyl Ester  -  - 48 9 52 11
Yellow Grease 2 Methyl Ester 46 8 43 6 34 1

Cloud Point: This represents the temperature at which the fuel begins to become visually cloudy; technically, this is the point where small solid crystals of fuel can be observed. The fuel can probably still be used at this point as long as the filters do not plug.

Pour Point: This is the temperature at which, basically, the fuel has gelled to the point where it will not flow. Related to vehicle operation, this measure is not as useful as the cold filter plugging point as the filters have already been plugged to the point when the fuel will not flow at all.

Cold Filter Plugging Point (CFPP): This is a more serious measure of cold flow properties. It is the temperature at which the fuel crystals have amassed in such quantities that they cause a test filter to plug. Most consider this to be a better measure of cold flow properties and of cold flow performance.

Simulated Filter Plugging Point (SFPP): This method resembles CFPP, but it is claimed to represent better the real cold operability than CFPP. The major differences between methods are the filter pore size and speed of temperature changes.

In the IEA-AMF Annex 10 (Nylund and Aakko, 2000), real starting temperature of an engine worsened by some 4 °C when 20% RME was added into diesel fuel, which was not indicated by the CFPP results. The cold flow improver additive substantially improved the cold starting performance of RME blend. However, CFPP overestimated the efficiency of cold flow additive in RME blend, whereas for regular diesel it depicted well the cold starting temperature. Another analysis method, SFPP, was a more reliable measure to depict the real starting temperature, (for RME blend with additive, CFPP was -21 °C, SFPP -12 °C and real starting temperature -15 °C. For diesel fuel with additive, the respective results were -14, -12, and -15 °C).

Cetane number

Generally, the cetane number of biodiesel can be affected by the choice of feedstock. Most of the biodiesel has cetane numbers higher than 47, in comparison to a lower limit for cetane number of 40 for highway diesel fuel in the ASTM D975-15 2-D grade, and respective limit of 51 used in Europe (EN 590:2014 standard). Thus biodiesel enjoys an advantage in cetane number over petrol-diesel in the U.S., but not in Europe. Highly saturated biodiesels, including those from animal fats and used vegetable oils can have very high cetane numbers, even as high as 70. In a sense this principle also applies to petro-diesel: paraffinic diesel yields high cetane number but poor cold properties, while aromatics are good for cold flow properties but not for cetane number. This issue is discussed also in the chapter of paraffinic fuels. Biofuels made from polyunsaturated feedstocks will generally have cetane numbers at the low end for biodiesel. Figures 5 and 6 below illustrate the varying cetane numbers and their feedstock makeup. Note that the nomenclature is Cxx:y – where xx is the number of carbon atoms in the feedstock and y is the number of double bonds. (IEA-AMF Task 34-1: McGill et al. 2008).

Figure 5. Variation in cetane number with feedstock (NREL, 2006)

Figure 6. Cetane numbers of petrol-diesel and biodiesel fuels from various feedstocks (NREL, 2006)


Distillation range of biodiesel esters is narrow. In addition, these esters are high-boiling compounds when compared to regular diesel fuel (Figure 7). This may lead into engine oil dilution and other problems as described in compatibility section.

Figure 7. Distillation curves of a typical diesel fuel (EN 590), FAME, HVO, and diesel fuel containing 30 vol-% HVO. (Neste 2016).

Sulfur and trace elements

Biodiesel esters are typically sulfur-free. However, they may contain trace elements that cause clogging of diesel particulate filters. In biodiesel esters, for example, potassium (K), sodium (Na), and phosphorus (P) may be present due to the feedstock or catalysts used in production process. Some of these elements are limited as such in the FAME standards, and also via (sulfated) ash analysis. (IEA-AMF Task 34-1: McGill et al. 2008).


Viscosity of FAME esters is high, and it increases with decreasing temperature (Figure 8). This may lead to problems when using FAME at cold temperatures.

Figure 8. Impact of temperature on RME and ULSD viscosity (Bannister et al. 2009)


Lubricity of FAME biodiesel is excellent. Biodiesel, even in small blend quantities, actually improves the lubricity of petroleum diesel fuels. This effect depends heavily on the lubricity of the petroleum diesel fuel into which the biodiesel is blended. Typically, winter grade diesel fuels have low lubricity. In recent years, the reductions required in fuel sulfur and aromatic content have also caused reductions in the lubricity properties. Furthermore, the process to remove sulfur and aromatics, namely hydrotreating, also removes other compounds that help to provide good lubricity qualities to the fuel. Lubricity can be improved with lubricity additives or by using FAME biodiesel. As little as 1 or 2% of biodiesel blended with ultra-low-sulfur (less than 15 ppm sulfur) diesel number 2 can improve the lubricity to acceptable levels. More biodiesel is required to bring the ultra-low-sulfur diesel number 1 up to acceptable levels, i.e. as much as 5 to 6%. Lubricity additives can also be used to improve the lubricity of ultra-low-sulfur diesel fuel. (Schumacher 2005, IEA-AMF Task 34-1 McGill et al. 2008).

Stability and water

Fuel aging and oxidation over a long term can lead to high acid numbers, high viscosity, and the formation of residues and sediments that eventually could clog filters. Many factors can influence the degree of instability of the fuel.

A fuel with a higher level of unsaturation will oxidize more readily than a fully saturated fuel. For example, biodiesel ester composed primarily of C18:3 is 100 times more unstable than a fuel made of C18:1. EN 14214 standard limits polyunsaturated acid methyl esters of FAME due to this reason. The iodine number limit reflects the total number of double bonds, and therefore fuels tendency to form sludge. Rancimat oxidations stability reflects only acid forming tendency of FAME (WWFC 2009). High molecular weight glycerides and glycerin, which may be present as remnants from production process, may also cause filter plugging and engine deposits. (IEA-AMF Task 34-1 McGill et al. 2008).

When oxidizing FAME it forms peroxides and acids, which can damage or degrade plastics, elastomers and metals (WWFC 2009) and this is one substantial drawback. Acids may also be present as remnants from production process.

Water accelerates oxidation, increases corrosion and promotes microbiological growth. Biodiesel esters are polar and hygroscopic compounds with affinity to water. Thus it is especially important to dehydrate FAME in the production and minimize the contact with water in every handling step (WWFC 2009).

Antioxidants, whether resulting from the feedstock oil or the manufacturing process or from the additives introduced down the line from biodiesel production, can help to protect the fuel against degradation over time. Many vegetable oils and fats are produced with natural antioxidants and they remain in the fuel unless certain processes such as bleaching are used at the end of the production. Those processes will remove the antioxidants. (IEA-AMF Task 34-1 McGill et al. 2008).

EN 14214 standard recommends that stabilizing agents should be added to FAME immediately after its production, and at least before blending with petroleum diesel fuel. However, WWFC (2009) points out that overuse of anti-oxidants can lead to the additional formation of sludge.