Our study describes the characteristics of growing and using both groups of plants (algae, tree species, short rotation coppices, and arable crops), as well as the potential savings to be achieved in terms of harmful gas emissions by comparing them to other biomass resources (arable crops, short rotation coppices). This paper briefly outlines the current significance of these crops, as well as their economic attributes, based not only on statistical data but also on our own experimental results.
Our results basically apply to Hungarian conditions, but the used methods and the specific technological and environmental data (applying one hectare areas) are suitable to international comparison. Hungarian specialties are highlighted for making comparison with international data.
In our calculations the main problem was a lack of detailed studies about typical forest technologies and their emissions in scientific papers, so in some cases we used trustworthy expert opinions in order to clarify the most important technical details about forestry. The results confirm that the average NPP of Hungarian forests is 10–46% higher than the EU average.
Due to the fact that forests represent a large amount of biomass and have long life cycles, while algae grows rather fast and can be used in multiple ways, they may have a significant impact on air pollutant emissions.
Forests are an irreplaceable national treasure and a form of land use that provides not only financial security but also mental refreshment, while also being indispensable aspects of environmental protection. A large proportion of their advantages cannot even be expressed in monetary terms.
1.3. Potential Significance of Algae
Algae have the highest potential yield in plants with the highest potential for CO
2 sequestration per hectare and—in the case of energy use through the avoided emissions from substituted fossil energy sources—also in CO
2 emissions reduction. Recently, microalgae have emerged as a source that can play a dual role in the bioremediation of wastewater, as well as the generation of biomass for energy and food production. Growing microalgae on different types of wastewaters has been studied over the past decades. The success of such studies depends on the performance of the selected microalgae strains [
41].
Since algae proliferate rather quickly, they can be grown in three-dimensional space and all of their parts can be used, so the amount of biomass to be harvested in one unit of a field (even up to 150–300 t ha−1) is many times that of field crops.
In order to produce this huge yield, algae use a vast amount of CO
2, which made it possible to purify the atmosphere millions of years ago; therefore, they may contribute to higher environmental, energy- and food security [
42]. The environmental impact of the algae plant can be observed in the purification of wastewater from mineral substances and the reduction of air pollutant emissions by means of CO
2 sequestration. Both of these impacts have significant economic implications since purified wastewater can be released into living waters without any risk (in theory, it can also be utilized for irrigation purposes), while the saved CO
2 emissions can theoretically be sold at the CO
2 stock exchange, especially to buyers who are interested in smaller quantities, mostly for marketing purposes (e.g., hypermarket chains, large companies operating fuel stations, organizers of international programs).
In order to reach outstandingly high yields, it is necessary to provide the ideal conditions needed for photosynthesis and growth (light, temperature, macro- and micronutrients, and carbon dioxide). Of these factors, the lack of CO
2 often causes limited yields, but the fundamental condition of a large extent of CO
2 sequestration is to make sure that both the proper concentration of CO
2 and all other conditions of intensive technology are available. As for light, the minimum light intensity is 3240 lx and at least 180 [
43] or 300 [
44] hours of effective illumination are needed to reach 500 mg L
−1. The optimum temperature is between 20 and 30 degrees Celsius [
45]. At the same time, low temperature within the optimum range increases yields and the solubility of CO
2 [
44].
The CO
2 sequestration ability of algae can be used mainly in power plants. The significance of power plants is shown by the fact that they produce more than 37% of Hungarian CO
2 emissions. Although emissions are constantly decreasing, they still remain at around 11.6 Mt year
−1. However, algae production makes it possible to capture CO
2 (and sell the CO
2 quota) and, in addition, to utilize power plant waste heat to produce a huge amount of algae biomass [
46]. From an environmental protection perspective, algae can be used even more effectively if connected to a biogas plant that performs wastewater purification, since the conventional process of oxidation currently calls for a significant amount of mechanical energy, which can be achieved with solar energy for algae.
Flue gases usually contain 5–30% CO
2, a level that is basically in accordance with the concentration tolerated by algae [
47]. The other gases present in flue gases (NO
x, SO
x, and C
xHy) can also affect the efficiency of the CO
2 sequestration activity of algae. For this reason, occasional purification is necessary before release into algae ponds [
48]. At the same time, there are algae species that are also able to capture these gases [
49] to a limited extent and under specific environmental conditions, but these are not the same as the most effective CO
2 sequestration algae.
Since algal species are diverse in composition, this diversity is reflected in their CO
2 sequestration abilities. However, according to our own experiments [
16], CO
2 fertilization of the examined algae species—with their rather diverse characteristics—resulted in nearly double yield increases independently of algae species, while it increased the protein content and decreased the oil content of algae.
The average composition of algae is described by Richmond [
50] as CO
2 0.48 H 1.83 N 0.11 P 0.01, while Chowdhury et al. [
51] provided the following formulae: C
106H
263O
110N
16P. The average composition of the dry matter of the most frequently used
Chlorella vulgaris species (which is also used in this experiment) is described by Becker [
52]: 50% protein, 15% carbohydrate, 25% lipids, and 10% other materials. Theoretically, the production of one kg of algae dry matter (with 50% carbon content) calls for 1.6–2 kg CO
2 [
17], while the N need fluctuates between 8 and 16 t ha
−1 year
−1 in the case of an average composition, which is 55–111 times that of rape [
53].
Algae plant technology also significantly affects the amount of CO
2 to be captured, as well as the potential algae yields. In the case of raceway ponds, the efficiency of CO
2 sequestration is around 10%, while it is around 35% in greenhouse technologies and even reaches 75% in photo-bioreactor (PBR) systems [
44]. The amount of CO
2 emitted during photorespiration reduces theoretical efficiency by 20–30% [
54].
According to Carlsson and Bowles [
18], potential algae yields in raceway ponds are 50–60 t ha
−1 year
−1 in dry material, while Chisti [
55], reports 127 t ha
−1 year
−1. Based on the same authors’ study the potential yields in PBR systems are 150 t ha
−1 year
−1 and 263 t ha
−1 year
−1, respectively. Bai et al. [
16] achieved a yield of 252–288 t ha
−1 in a 14-day-long rotation in small-scale field experiments with the use of
Chlorella vulgaris (
Beijerinck), under the following optimal circumstances:
3.84 g wet weight/500 mL (C. vulgaris) of inoculums solution
28-day measurement interval (from 9 July to 6 August 2010)
1000 L tanks, 500 L of water, 30 cm water depth
Natural illumination (14–15 h/day)
Outdoor temperature (17–29 °C daily average temperature, min. 14 °C, max. 35 °C, 28-day average: 24.5 °C)
No added manure and carbon dioxide; instead, we used 250, 500, and 1000 mL nutrient solutions with 0.42 mg/L nitrogen, 0.18 mg/L phosphorus, and 0.402 mg/L potassium on the basic case (250 mL)
Moderate aeration: 50 L/h and without aeration in each of the nutrient level
In the study by Lam et al. [
56], diluted wastewater was used in cultivation.
Chlorella vulgaris was able to grow under the following conditions: 0.02–0.2
v/v of domestic wastewater, initial pH of 3–9, and 0.03
v/v initial amount of microalgae seed. Under these conditions, the highest lipid content reached 32.7% during 2–12-day-long cultivation times. During 12 days under pH 3 or 7, 0.02
v/v wastewater concentration (optimum parameters), the biomass yield reached 0.5 g/L.
Chinnasamy et al. [
57] obtained a dry weight production of about 50 µg mL
−1 during the exponential phase of
C. vulgaris grown at 0.036% CO
2 and 30 °C, which falls within the values (13–54 µg mL
−1) obtained in Chia et al. [
58]. The experiments were carried out in 500-mL polycarbonate Erlenmeyer flasks containing 200 mL of culture kept semi-continuously under controlled conditions of light intensity (150 µmol m
−2 s
−1), light-dark cycle (16:8 h), and temperature (20 + 2 °C).
CO
2 concentration has an impact on the efficiency of sequestration. If the concentration of CO
2 is less than optimal, it directly decreases potential yields, while a higher than optimal concentration has an indirect yield reduction effect due to the acidification of the algae system. In the case of
Chlorella vulgaris, the algae species used in our experiments [
16], the optimal CO
2 concentration is around 20%, based on the data from 37 developed countries [
45,
57]. In the case of
Nannochloropsis [
22,
59] and
Chlorococcum species [
60] much higher values (even up to 40%) were obtained. For the strains
Botryococcus braunii SI-30,
S. obliquus SJTU-3 and
C. pyrenoidosa SJTU-2, which are quite promising for biofuel production, a CO
2 concentration of 30–50% can be deemed ideal [
61]. Hirata et al. [
62] determined the optimal daily CO
2 dose of
Chlorella vulgaris as 865 mg L
−1, while Murakami and Ikenouchi [
63] concluded the optimum is 1 g L
−1 in the case of the
Chlorella sp. UK001 strain.
Theoretically, algae are able to directly capture the CO
2 emitted by fossil fuels. Based on the experiments performed by Taştan et al. [
64], an algae biomass yield of anything up to 1.3–1.6 g L
−1 day
−1 can be achieved under an optimal concentration of diesel and algae, which could potentially result in 2.4–3.7 g L
−1 CO
2 sequestration per day. This could possibly have a huge potential impact if the necessary technical and economic conditions needed for the technology could be established on a large scale and worldwide.
The energetic efficiency and CO
2 balance of algae for biodiesel production were examined by Slade and Bauen [
44]. The findings clearly show that PBR systems may have a higher energetic efficiency, but they have much higher CO
2 emissions than open water algae systems and fossil energy resources. The higher CO
2 emission is mainly due to the significant amount of electricity needed, which could theoretically be zero if produced from renewable energy sources. According to Jonker and Faaij [
65], prominent elements of the energy consumption ratios of algae production are CO
2 supply for raceway ponds and circulation power consumption for horizontal tubular systems.
As regards the purpose of algae production, the calculations of Soratana et al. [
66] showed that the impact of utilization for biodiesel production purposes (0.9–1 kg GHG MJ
−1) on emissions saving is around twice as much as that of methane production. At the same time, drying may result in significant energy needs and air pollutant emissions, therefore, there could be a significant difference between the CO
2 emissions of wet and dry algae-biomass (1–8 kg CO
2 equi GJ
−1 [
67], and 20–50 kg CO
2 equi/GJ [
68]). At the same time, wet algae with 5–14% dry matter content [
69] is suitable for anaerobic fermentation, but is unsuitable for any other use.
Around half of the air pollutant emissions during intensive algae production take place at harvesting [
66]; therefore, choosing the most appropriate harvesting method is of great importance. At the same time, dewatering and drying are significant factors in emissions, so great savings can be achieved by using energy-efficient methods and renewable energy. Even though solar drying would be the most obvious solution [
66,
70], it has a large space need [
71] and the oxidation of lipids may deteriorate the quality of the algae [
72]. Based on Chowdhury et al. [
51], the integration of technology can lead to 3–14 GJ t
−1 biodiesel energy (and the related pollutant) savings.
During biodiesel production the common efficiency of oil extraction and esterification (using hexane and methanol) is between 0.55 and 1, and the mean value is 0.9 according to Collet et al. [
69], who processed 41 sources. Soratana and Landis [
68] prepared a study which examined 20 technological variations and concluded that the emissions from PBR production had an algae dry matter range between 0.02 and 0.09 kg CO
2 equi kg
−1, considering the utilization of by-products and calculating with 30% oil content
Chlorella vulgaris and a specific algae dry matter value of 1.85 kg CO
2 kg
−1. Together with harvesting, dewatering and drying, emissions of the PBR system range between 0.4 and 1 kg CO
2 equi kg
−1 algae dry matter, according to Clarens et al. [
67]. Gnansounou and Raman [
73] characterized the emission of biodiesel production from algae with the following values, with similar technical parameters as the cases described above:
biodiesel and protein feed production: 0.22–0.39 CO2 equi kg−1 algae dry matter
biodiesel, protein feed and succinic acid production: 0.33–0.46 42 kg CO2 equi kg−1 algae dry matter
When using wastewater feedstock (e.g., biogas plant), the emissions savings resulting from the saved energy used for feedstock during the fertilization of algae (nitrogen: 14 MJ kg
−1 N, phosphorus: 24 MJ kg
−1 P [
74]) is also a part of the lifecycle analysis.
In extensive algae pond systems, the amount of CO
2 emitted during algae production is negligible, amounting to only 2% of the emissions during the whole life cycle [
75], while its extent is 9% in the case of PBR systems [
76]. The electricity needs when injecting CO
2 from flue gases into the algae pond is somewhat less, but must definitely be taken into consideration (0.08 MJ kg
−1 CO
2 [
77]). In raceway ponds, one also has to consider the loss of a part of the injected CO
2; according to Collet et al. [
69], the average amount of this loss is 18%.
With regard to economic implications, it is a significant fact that the harvesting of algae can—ideally—be carried out every two weeks, which represents a constant income and the continuous operation of processing plants with a short term inventory. There are no crop rotation problems and the acquisition of different investments is not necessary either, since the technological processes of algae species intended for economic utilization are the same. At the same time, the process itself is still expensive: estimates from Demirbas and Demirbas [
78] show—assuming 30% oil content algae and freely available flue gas—that the prime cost of algoil was 1.8 USD L
−1 in open systems and 1.4 USD L
−1 in PBR systems in 2010 [
78]. For cost comparison, it must be emphasized that the prime cost of biodiesel produced from palm oil, which is the cheapest vegetable oil, was 0.66 USD L
−1 in 2010 [
78]. According to Norsker et al. [
79], the 2010 production costs of algae dry matter were 4.95 € kg
−1 in raceway ponds, 4.16 € kg
−1 in horizontal tubular PBR systems and 5.96 € kg
−1 in flat panel PBR systems for 100 ha production size. As regards investment costs [
80], the typical investment range of raceway ponds is 200–300 thousand € ha
−1 based on several case studies, while for PBR systems it is 1000–3000 € ha
−1, depending primarily on the technology applied and the scale. Other previous calculations [
81] show that the 2010 investment costs of greenhouse pond systems were about 500 thousand € for 1 ha and 140 thousand € for 0.21 ha.