1. Introduction
In the agriculture and the agri-food industry in Poland, more than 10 million tonnes of waste is generated annually, most of which is subject to management, but the problem of inappropriate waste management is becoming increasingly apparent [
1].
The uncontrolled decomposition of waste from agriculture and the agri-food industry (PRS) increases the number of pollutants, including hazardous compounds and substances. For this reason, it becomes necessary to create new, rational processing systems from the agri-food industry and agriculture [
2].
One of the ways to manage the waste of plant origin is its processing in pressure agglomeration into granules or briquettes, which is confirmed by numerous scientific works [
3,
4,
5,
6].
The basic raw material for the production of pellets is sawdust [
7]. This is because, before the wood cutting process, the debris is removed by removing the bark and washing the logs. Which makes sawdust an ideal raw material for the production of pellets [
8].
In the case of pellets or briquettes, other waste materials are used increasingly frequently, e.g., waste from the fruit and vegetable industry.
According to Wandrasz [
9,
10], the composition of fuels created in the process of pressure agglomeration may include waste from the processing of oilseeds, walnut husk, and rapeseed pomace.
The aim of this study was to attempt to develop a technology of management for energy purposes of waste from the dairy industry, used as an additive in the process of pelleting with wood sawdust. As part of the work, the most advantageous material (composition and moisture of the mixture), process and construction parameters from the point of view of energy consumption of the process, and the quality of the obtained pellets were determined.
2. Materials and Methods
The basic raw material used for the research was sawdust from the BSH DĄBROWSCY SP. J., to which we added post-flotation dairy sewage sludge from the treatment plant operating in the MLEKOVITA plant in Wysokie Mazowieckie.
The research was divided into two stages. In the first stage, the physical and chemical properties of the tested materials were examined, including humidity, sawdust sieve analysis, and sawdust bulk density. In the second stage, the pelleting process of wood sawdust mixtures with the addition of 10, 15, and 20% of floating dairy sewage sludge was carried out, and the properties of the obtained granulate were determined, including kinetic strength, physical and isolated density, as well as its combustion heat and calorific value (
Table 1).
3. Results
Based on the conducted research, it was found that the raw material (sawdust), which was used during the research, was characterized by a humidity of 10.87%, while post-flotation sewage sludge was characterized by a humidity of 83.58%. Such a low moisture content of sawdust prevented them from being pelleted and us to obtain granules of the desired quality. The solution to this problem is to add an additive with high moisture content to the sawdust, which is post-flotation sewage sludge.
The study of the grain size distribution of sawdust allowed us to state that the largest percentage in this raw material was the fraction of 1.00 mm (35.94%). The 2.00 mm fraction (20.96%), the 0.50 mm fraction (16.56%), and the 4.0 mm fraction (9.64%) had a slightly smaller share. The smallest percentage, 0.016%, was the non-screen fraction with a size <0.063 mm.
Table 2 shows the effect of the content of post-flotation dairy sewage sludge in the mixture with sawdust on the course of the granulation process (demand of the granulator for the power recorded in the process of granulation of the mixture) as well as the physical and bulk density and the kinetic strength of the granulate.
On the basis of the conducted research, it was found that the mixtures with the addition of post-flotation dairy sewage sludge were characterized by increased susceptibility to granulation, which reduced the energy consumption of the granulation process of mixtures with its participation from 4.19 kW (compare to the sawdust granulation) to 2.87 kW (with 20% addition of sludge) and had a positive effect on the kinetic strength and density of the obtained granulate. Increasing the content of post-flotation dairy sewage sludge in the mixture with sawdust from 10 to 15% increased the kinetic strength of the granulate from 98.30% to 98.95%. Further increase in the post-flotation additive of dairy sewage sludge from 15 to 20% resulted in a slight decrease in the kinetic strength of the granulate from 98.95 to 96.85%.
Increasing the content of post-flotation dairy sewage sludge in a mixture with sawdust from 10 to 20% caused a decrease in granulate density from the value of 1224.74 kg/m3 to 1186.70 kg/m3. Along with the increase in the content of sludge addition, the bulk density of the granules slightly decreased in relation to the granules obtained alone.
The obtained values of the heat of combustion and the calorific value prove that the addition of post-flotation dairy sewage sludge only slightly reduces the energy values of the produced pellets. For example, the addition of 10% of post-flotation dairy sewage sludge to sawdust caused a decrease in the heat of combustion by approx. 0.698 MJ/kg (approx. 3.46%) from the value of 20.199 to 19.500 MJ/kg and a decrease in the calorific value by approx. 0.685 MJ/kg (3.7%) from the value of 18.541 to 17.856 MJ/kg.
4. Summary
On the basis of the conducted tests, the properties of the raw materials used in the tests, i.e., sawdust used in the BSH DĄBROWSCY SP. J. and post-flotation dairy sewage sludge) and the properties of the obtained granulate were determined (physical density, bulk density, and kinetic strength of the granulate, as well as the heat of combustion and its calorific value). The conducted research on the granulation process allowed us to determine that the mixtures with the addition of post-flotation dairy sewage sludge were characterized by increased susceptibility to granulation, which reduced the energy consumption of the granulation process of mixtures due to its participation and had a positive effect on the kinetic strength and density of the obtained granulate.
A positive aspect of the use of post-flotation dairy sewage sludge is the possibility of managing large amounts of post-production waste, which is often not used and left lying in company yards, which is why the plant is often forced to utilize them. The possibility of managing the post-flotation waste of the dairy industry by using it for the production of pellets is in line with the EU policy on waste management.
Author Contributions
P.C.: research, research analysis, preparation of the manuscript; S.O.: research concept, experiment design, research methodology, and manuscript correction; M.K.-S.: research analysis; M.K.: research analysis, performing research, G.S.: research analysis, performing research. All authors have read and agreed to the published version of the manuscript.
Funding
The work was carried out as part of a team project no. WZ/WB-IIS/2020 and ´ financed by the Polish Ministry of Science and Higher Education.
Institutional Review Board Statement
Not applicable.
Informed Consent Statement
The study did not involve humans.
Data Availability Statement
Not applicable.
Conflicts of Interest
The authors declare no conflict of interest. The founding sponsors had no role in the design of the study; in the collection, analyses, or interpretation of data; in the writing of the manuscript, and in the decision to publish the results.
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Table 1.
Methods.
Parameter | Methodology |
---|
Granulate bulk density | PN-EN ISO 17828:2016-02 |
The kinetic strength of the granules | PN-EN ISO 17831-1:2016-02 |
Physical density | With the use of a caliper and an AS 220/C/2 laboratory balance by RADWAG |
Humidity | PN-76/R-64752 |
Particle size distribution | PN-89/R-64798 |
Combustion heat/calorific value | KL-12Mn calorimeter |
Table 2.
Influence of the content of post-flotation sewage sludge on the granulation process.
Table 2.
Influence of the content of post-flotation sewage sludge on the granulation process.
Sediment Content [%] | Power Requirement of the Granulator [kW] | Quality of Pellet |
---|
Kinetic Strength [%] | Physical Density [kg/m3] | Bulk Density [kg/m3] |
---|
0 | 4.19 | 95.07 | 1301.05 | 618.04 |
10 | 3.92 | 98.30 | 1224.74 | 545.23 |
15 | 3.54 | 98.95 | 1216.78 | 526.48 |
20 | 2.87 | 96.85 | 1186.70 | 430.55 |
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