1. Introduction
A recent study on timber trade in the World, based on FAO statistics [
1], revealed a rising trend in the use of the wood for various markets, especially in response to energy demand [
2]. Because of increasing crude oil prices, the limited availability of fossil fuels and the deterioration of environmental quality due to greenhouse gases, mainly CO
2, various biomass solid materials have recently been proposed for use as fuels [
3].
According to the analysis carried out by the European Renewable Energy Council, the EU aims for a 100% renewable energy future by 2050, where biomass will potentially supply about 36% of the total European primary energy consumption, while the potential for many developing countries is higher since their resources in such areas are larger [
4,
5].
The versatile nature of wood biomass fuels is both a main asset and a significant obstacle at the same time. On one hand, wood biomass is available in many forms and in all parts of the World, allowing the deployment of bioenergy almost everywhere, once the useful sources have been identified and assessed [
6]. On the other hand, this same diversity makes biomass a complex and difficult fuel.
Wood is still the dominant source of fuel in many developing countries. Until now, about 15% of world energy requirements are provided by biomass. About 13% of wood fuels is used in developing countries, while 2% is used in developed countries [
7]. Among the many methods of potentially sustainable energy generation in the latter countries, biomass has been receiving increasing attention. Among the biomass sources that may be used for energy production, wood shows the greatest potential from both the productive and environmental point of view [
7].
The quality of the wood fuel varies according to site characteristics, harvesting season and silvicultural treatment. Moreover, because of high moisture content, irregular shape and size, and low bulk density, woody biomass is very difficult to handle, transport, store, and utilize in its original form. These are the main reasons of interest in determining the relationship between the origin of the wood fuel and such main quality characteristics as: particle-size distribution, bark content and calorific value. Particle-size distribution is crucial to fuel handling efficiency, to its drying and reaction rate, to the energy required for conversion into ethanol, and to the yield of bio-oil obtained from pyrolysis. Bark has a high ash and alkali metal content, which causes corrosion and sintering of the boilers, although the ash content in tree bark is 4–5 times lower than in than seen in straw and other herbaceous crops [
6]. A high bark to fiber ratio has a crucial and negative effect on pulping, as well as on heating value the latter related to the higher moisture content of bark compared to fiber. A high bark content also has a significant impact on pelletizing potential and pellet durability. Calorific value is an essential quality for any fuels, and is relatively constant for wood fuels in their dry status [
6].
Transformation of woody biomass materials into pellets, briquettes, or chips reduces costs and problems with handling, transportation, storage, and utilization of low bulk density biomass materials. Among the various transformation methods tried one in particular—chipping—seems to have achieved a good compromise. Comminution (or chipping) is an essential element of all modern energy wood chains, because automated boilers only accept homogeneous fuel particles within specified size limits. Furthermore, comminution may offer additional benefits in terms of increased load density and improved handling quality [
8].
Wood chips can be obtained from various agricultural, forestry or industrial practices. In this paper we focused on two main production types: forestry and agroforestry. In the forestry practices we analyzed the chips produced by the full tree harvesting system (FTS) from coniferous woods and by the logging residues (LR) from the coppice. These are the more interesting forest production sources from the economic and technical point of view for Italian wood chip production. Addressing logging residues is a good practice for fire prevention and in many cases creates a favorable environment for agroforestry and forest plantations by reducing the difficulty of the regeneration work and improving the quality and productivity of the site preparation and planting work [
9,
10].
In the agroforestry practices we analyzed only the short rotation coppice (SRC) for wood chip production. The specialized plantations for woody biomass production can be defined as short rotation coppice when they have high density (8,000–15,000 stumps/ha) and short harvesting intervals (2–5 years). SRC for energy purposes is rapidly expanding in Europe because of the reduced dependence on foreign sources of energy and the availability of large areas of set-aside agricultural land [
11]. Energy crops appear as a promising option for ensuring feedstock. The profitability of energy crops is highly dependent on an appropriate logistics, logging scheme, and specially, crop yields [
12,
13].
In this research we set out to determine the particle-size distribution, the fiber, the bark and the leaves content, the heating value, the CNH and the ash content of a wide sample of woodchips, collected from 10 forestry and 10 agroforestry production types in Italy. This sample was chosen to represent a cross-section of the Italian fuel chip production, and focused on two main production types: forestry (full tree harvesting, logging residues) and agroforestry (short rotation coppice). For the forestry production chips from coniferous (Pinus spp. and Picea abies L.) and broadleaves (Quercus spp. and Fagus sylvatica L.) were examined. For the agroforestry production wood chips from poplar plantations (five different clones with two different harvesting intervals) were analyzed. The main aim was to evaluate the wood chip energetic characteristics for their rational use for energy purposes.
2. Materials and Methods
Twenty yards for wood chips production in Italy, 10 in forest sites and 10 in agroforestry, were sampled. All these yards were for fuel wood production. This sample was selected to represent a cross-section of the Italian fuel chip production, and focused on two main production types: forestry (FTS, LR) in
Table 1 and agroforestry (SRC) in
Table 2. For the forestry production there were wood chips from coniferous (
Pinus spp. and
Picea abies L.) and broadleaves (
Quercus spp. and
Fagus sylvatica L.). These two productions sources, though obviously stemming from traditional forestry activities, in reality they also differ in three main aspects that affect differently the chip quality. The first difference concerns the tree types considered from the two production types, in “LR” broadleaves (hardwood) and in “FTS” coniferous species (softwood). This difference has a strong impact on heating value and other chip characteristics. The second difference concerns the content of leaves, “LR” contains no leaves, because it consists of coppice branches harvested in winter, when no leaves are present, whereas “FTS” contains significant amounts of leaf material because it consists of conifer trees. The third difference concerns the bark content, “LR” consists of small tree parts (branches), whereas “FTS” includes the entire tree, with an obvious effect on the bark to fiber ratio.
Table 1.
The experimental matrix of 10 different forestry yards.
Table 1.
The experimental matrix of 10 different forestry yards.
Types | Main trees | Code | Samples | Average DBH cm ± SD |
---|
FTS | Picea abies L. | a | 20 | 15.6 ± 1.1 |
FTS | Picea abies L. | b | 20 | 16.5 ± 1.9 |
FTS | Pinus nigra Arn. | c | 20 | 22.1 ± 1.5 |
FTS | Pinus pinaster Ait. | d | 20 | 23.3 ± 2.1 |
FTS | Pinus halepensis Mill. | e | 20 | 16.6 ± 0.9 |
Types | Main trees | Code | Samples | Average topping diameter cm ± SD |
LR | Quercus cerris L. | a | 20 | 8.2 ± 1.3 |
LR | Quercus pubescens Willd. | b | 20 | 8.1 ± 1.0 |
LR | Quercus cerris L. | c | 20 | 9.6 ± 1.6 |
LR | Fagus sylvatica L. | d | 20 | 8.2 ± 1.1 |
LR | Fagus sylvatica L. | e | 20 | 7.6 ± 0.8 |
Table 2.
The experimental matrix of 10 different agroforestry yards in SRC plantation.
Table 2.
The experimental matrix of 10 different agroforestry yards in SRC plantation.
Harvesting interval | Poplar clones | Code | Samples |
---|
2 years | AF2 | a | 20 |
3 years | AF2 | a | 20 |
2 years | AF6 | b | 20 |
3 years | AF6 | b | 20 |
2 years | Monviso | c | 20 |
3 years | Monviso | c | 20 |
2 years | Monviso | d | 20 |
3 years | Monviso | d | 20 |
2 years | Muur | e | 20 |
3 years | Muur | e | 20 |
For the agroforestry production there were wood chips from poplar plantations (different clones with two different harvesting intervals). For each site 20 chip samples were randomly collected and each sample consisted of approximately 1 kg of chips, which were put in individual bags, and duly tagged in order to identify the type and provenance. Sampling aimed at providing a representative cross-section of current operations and did not follow in detail any specific design to balance treatments for comparative purposes. For the forestry yards, the FTS sample types were obtained from first thinning of coniferous woods (range of age 27–35 years), while the LR sample types were obtained from broadleaved logging residues of final coppice cuts (range of age 19–30 years). Logging residues consisted of tops and branches, left after the harvesting of adult trees from final cuts. For the 10 agroforestry yards for the four clones, two harvesting intervals were selected, the 2 years interval and the 3 years one. In all the yards the samples had been processed with the same chipper, an industrial chipper assembled on a truck with a drum unit. This machine was equipped with an independent engine (power 100 kW) and hydraulic crane. This was important because chipper characteristics have been shown to significantly affect particle-size distribution and chips quality [
14].
The samples were analyzed for: (1) component breakdown, (2) particle-size distribution and (3) higher heating value (HHV), (4) content of Carbon (C), Nitrogen (N) and Hydrogen (H) and (5) ash content. Each of the 400 samples was divided into five sub-samples with different masses. For the analysis (1) each sub-sample was 0.2 kg, while for the analysis (2) each sub-sample was 0.5 kg and for the analyses (3–5) each sub-sample was 0.1 kg. The sub-samples were randomly extracted from the larger pool of original samples.
Component breakdown was determined on 200 g sub-samples, by manually separating their content into the following main components: fiber, bark, twigs, leaves, dust and other [
14]. Each component was weighed with an Orma (model BC16D) precision scale. Particle-size distribution was determined on 500 g subsamples, according to CEN/TS 15149-1:2011 “Solid biofuels—Determination of particle size distribution—Part 1: Oscillating screen method using sieve apertures of 1 mm and above”, using a certified model FTL0200 automatic screening device. Five sieves were used in order to separate the six following chip length classes: >100 mm, 100–63 mm, 63–45 mm, 45–16 mm, 16–3.15 mm, <3.15 mm. Each fraction was then weighed with the Orma (model BC16D) precision scale.
According to the European Standard UNI EN 14918:2010 “Solid biofuels—Method for the determination of calorific value”, for the measurement of the higher heating value a sub-sample of 100 g was ground with an Ika Werke MF10B rotating-blade mill equipped with a 0.7 mm sieve, then 1 g of wood dust was selected and compressed into pellets with a Parr manual press. The pellet was burned in a Parr 6200 adiabatic bomb calorimeter.
According to the European Standard UNI EN 15104:2011 “Solid biofuels—Determination of total content of carbon, hydrogen and nitrogen—Instrumental methods”, the content of C, H, and N was determined in a sub-sample of 100 g. Biomass content of C, H and N was analyzed in a Leco CHN 1000 elemental analyzer by the LECO-1 method using a combustion analyzer.
Standard ash was prepared according to UNI EN 14775:2010 “Solid biofuels—Determination of ash content”. The fuel sub-sample of 100 g was ground with an Ika Werke MF10B rotating-blade mill equipped with a 1 mm sieve. Then, only 50 g was placed in a laboratory furnace in such a way that the sample loading did not exceed 1.0 kg/m2. The furnace was heated to 250 °C at a rate of 0.083 °C/s. The sample was left at this temperature for 1 h to allow devolatilization before ignition. Afterwards, the furnace was heated at 0.083 °C/s to 550 °C. The sample was maintained at this temperature for 2 h, removed from the furnace, cooled in ambient air for approximately 5 min, then transferred to a dessicator and after cooling to ambient temperature, weighed.
Data were analyzed with the Statistica 2010 advanced statistics software, in order to check the statistical significance of the eventual differences between treatments with ANOVA and MANOVA techniques. Post-hoc tests were conducted with Tukey HSD test method.