Process monitoring
Temperature: Temperature is a widely used parameter to describe the composting process behavior (Waqas et al., 2018). Figure 1 shows the temperature profiles of treatments. Table 3 summarizes the time required in each treatment to reach the thermophilic phase and its length, maximum temperature, time to reach environmental temperature, and the total amount of water added during the humectation phases.
Table 3
Temperature behavior in each replicate per treatment
Treatment
|
Time to the start of the thermophilic phase (days)
|
TMAX (°C)
|
Time to TMAX (days)
|
Duration of the thermophilic phase (days)
|
Time to TENV ± 3°C from process start (days)
|
Added water (L)
|
pH - initial
|
pH final
|
TA
|
2
|
57.3
|
4
|
17
|
54
|
72.0
|
8.4
|
8.9
|
TB
|
2
|
57.0
|
4
|
17
|
49
|
75.3
|
8.4
|
8.8
|
TC
|
2
|
33.3
|
3
|
0
|
47
|
78.7
|
8.5
|
8.7
|
Note: TA: Treatment A; TB: Treatment B; TC: Treatment C; TMAX Maximum temperature, TENV environmental temperature. |
Treatments A and B had a typical behavior of the composting process, with sequential mesophilic, thermophilic, cooling, and maturation phases. According to Soobhany (2018), the thermophilic phase starts at temperatures higher than 45°C. This condition was achieved on the second day of the process, in agreement with results from Waqas et al. (2018) in biowaste composting and Rizzo et al. (2013) in the composting of chicken manure. These results are associated with the predominance of readily biodegradable polymers present in substrates such as carbohydrates, proteins, and amino acids from the Bw, and CM and due to the action of microbial consortia, which increase heat generation with the consequent temperature growth. On the other hand, treatment C (70% So and 30% Wc) did not reach temperatures over 45°C, which is associated with the characteristics of SO tending to acidity, which could affect the biodegradation kinetics of the present TOC and consequently heat generation; furthermore, the low C/N ratio (15) in this treatment, the storage period of SO (1 month) and thus, certain degradation degree, could have limited the biological activity.
Regarding sanitization, the treatments did not reach temperatures above 65°C, which is the recommended temperature for disinfection and destruction of larvae and insect seeds (Waqas et al., 2018). However, treatments A and B showed, for at least three consecutive days, temperatures above 55°C, which according to Hemidat et al. (2018), allow pathogen destruction; in addition, no statistically significant differences were found between treatments (p = 0.081). On the other hand, treatment C did not fulfill this condition, for which it could represent a potential risk if directly applied to the soil (Lasaridi et al., 2006). The maximum temperature was achieved in treatments A and B, in both cases with 57°C (Table 2), and in an average time of four days. The length of the thermophilic phase was 17 days in both treatments, which indicates process efficiency (Cáceres et al., 2016).
Figure 1 here
The cooling phase started between process days 19 and 21 in all treatments. Treatment B achieved a temperature closer to ambient (10 ± 5°C) in lower time (49 days) compared to treatment A (54 days), with statistically significant differences between the treatments (p = 0. 035). This behavior could be associated with a higher organic matter content in treatment B due to the fraction of CM that provides TOC, TN, and nutrients that stimulate biological activity. This shows that the mixture of CM and SO (Treatment B) reduces the processing time compared to the mixture of CM, Bw, and SO (Treatment A), which could have lignocellulosic components coming from the Bw that could increase processing time. These results are similar to those from Hemidat et al. (2018) in the composting of Bw, indicating that materials with cellulose and lignin take longer to degrade.
pH: The pH allows following process conditions; in the first phase, a typical pH decrease occurred linked to the high rate of organic matter degradation that generates organic acids and CO2. Figure 2 shows the pH dynamics in each treatment. At the start of the process, pH was alkaline (> 8) in all treatments due to the presence of CM in all the mixtures; however, as the process continued, a slightly pH decrease happened in all treatments due to the generation of short-chain fatty acids as intermediate products of the bacterial metabolism of the organic matter degradation. The higher pH values during the process were obtained in treatments A (10.19) and C (10.00), both on day 46. These results show statistically significant differences (p = 0.041) compared to the maximum pH in treatment B (9.77). The rapid pH increase during the thermophilic phase could be related to the release of ammonia as a result of protein degradation in the treatments for the presence of Bw and CM (Rizzo et al., 2013; Cáceres et al., 2016), the decomposition of organic acids and the release of CO2 during pile turning (Waqas et al., 2018).
During the cooling phase, pH values tended to decrease in treatment B, which can be linked to the production of organic acids during the decomposition of OM from CM and the nitrification process (Rizzo et al., 2013). However, at the process end, all treatments had pH in the alkaline range (higher to 8.0), treatment A with the highest values, although there were no statistically significant differences with treatments B and C (p = 0.54). Typically, pH follows a behavior pattern in the composting process characterized by low levels in the first stages and higher levels in the last stages (Waqas et al., 2018)
Figure 2 here
Electric conductivity: Electric conductivity reflects the concentration of water-soluble inorganic ions in the compost (Bernal et al., 2017). Figure 3 shows the EC behavior in the treatments. EC was higher (EC > 2 mS/cm) at the process start in treatments A and B associated with the predominance of CM, which contains salts such as sodium and calcium. A generalized trend was observed in these treatments of an increase in EC with a slight decrease concurring with the days when treatments were moisturized, thus promoting the leaching of salts. According to Gong et al. (2017), the EC increase is due to microbial mineralization of organic matter and the release of mineral ions such as phosphates, ammonia, and potassium during this process. In contrast, treatment C showed the lowest EC values related to the low EC from both SO and Wc at the process. It gradually decreased processing time, maintaining a range of relatively low values between 0.27 and 0.67 mS/cm. At the end of the process, treatments A and B had statistically equal EC values, and higher compared with treatment C (EC > 4.5 mS/cm).
Figure 3 here
End product quality
Physicochemical characteristics: Table 4 presents the end product quality obtained from the different treatments and its comparison with NTC 5167. Water content from treatment A had statistically significant differences (p = 0.048) with treatments B and C. B and C were not statistically different (p = 0.06). However, the water content in all treatments was higher to 50%, which is a value above recommendations from NTC 5167 (< 35%) and NCH2880 from Chile (30–45%); in addition, it was higher compared to values reported from some European Union countries (Cesaro et al., 2015). Although high water content in a stabilized process does not represent an end product quality problem, it could impact marketing and sales. An alternative to handle the water content values could be increasing turning in the maturation phase or implementing other processes such as solarization under controlled conditions to dehydrate and remove water (Jiang-ming, 2017).
Table 4
Physicochemical parameters from the compost obtained in each treatment
Parameter
|
Treatment A
|
Treatment B
|
Treatment C
|
NTC 5167
|
Water content (%)
|
56.1 ± 2.1 a
|
52.3 ± 3.6 b
|
47.5 ± 3.2 b
|
< 35
|
pH (%)
|
8.9 ± 0.2 a
|
8.6 ± 0.1 a
|
7.9 ± 0.1 b
|
> 4-<9
|
Density (g/cm³)
|
0.2 ± 0.1 a
|
0.2 ± 0.1 a
|
0.3 ± 0.1 a
|
< 0.6
|
WRC (%)
|
287.3 ± 26.3 a
|
322.7 ± 44.8 b
|
317.3 ± 37.0 b
|
> 100
|
CEC (meq/100 g)
|
51.3 ± 3.0 a
|
52.9 ± 3.3 a
|
44.1 ± 1.5 b
|
> 30
|
EC (mS/cm)
|
4.6 ± 0.6 a
|
4.5 ± 0.8 a
|
0.5 ± 0.4 b
|
-
|
Ashes (%)
|
18.2 ± 1.3 a
|
25.0 ± 2.2 a
|
27.5 ± 3.6 a
|
< 60
|
TOC (%)
|
38.0 ± 1.8 a
|
35.5 ± 1.8 a
|
36.0 ± 0.9 a
|
> 15
|
TN (%)
|
1.7 ± 0.1 a
|
1.6 ± 0.1 a
|
0.6 ± 0.1 b
|
> 1
|
C/N ratio
|
22.5 ± 2.0 a
|
21.7 ± 1.9 a
|
57.7 ± 2.9 b
|
-
|
TP (%)
|
0.7 ± 0.2 a
|
0.7 ± 0.1 a
|
0.1 ± 0.1 b
|
> 1
|
TK (%)
|
2.1 ± 0.4 a
|
2.1 ± 0.1 a
|
0.7 ± 0.1 b
|
> 1
|
Total Ca (%)
|
1.8 ± 0.5 a
|
1.9 ± 0.2 a
|
1.5 ± 0.9 a
|
-
|
Total Mg (%)
|
0.4 ± 0.2 a
|
0.5 ± 0.1 a
|
0.1 ± 0.1 a
|
-
|
Total Na (%)
|
1.0 ± 0.1 a
|
1.1 ± 0.1 a
|
0.9 ± 0.1 a
|
-
|
Total Zn (%)
|
0
|
0
|
0
|
-
|
FI
|
4.3 ± 0.1 a
|
4.3 ± 0.3 a
|
2.5 ± 0.1 b
|
|
Note: CEC. Cation Exchange Capacity, TOC. Total Organic Carbon, EC. Electric Conductivity, WRC. Water Retention Capacity, TN. Total Nitrogen. FI: Fertility Index |
Letters a and b indicate statistically significant differences (p < 0.05) between treatments. Treatments with the same letter did not show statistically significant differences. |
According to Sundberg and Jönsson (2008), the final pH of compost is highly dependent on substrates, composting process, and addition of amendments. Lasaridi et al. (2006) propose the pH range for the end product between 6.0 and 8.5 to allow the product to be used in various plants, while NTC 5167 recommends pH values between 4.0 and 9.0. All treatments fulfilled this requirement set by the Colombian regulation, treatments A and B having statistically significant differences to treatment C (p = 0.022). The pH increase up to alkaline values could be attributed to the consumption of protons during the decomposition of volatile fatty acids, generation of CO2 and mineralization of TN ( Cáceres et al., 2016).
Regarding density, all treatments had values lower to 0.6 g/cm³, which is the value recommended by the NTC 5167, Treatment C being higher (0.30 g/cm³), without statistically significant differences with treatments A and B (p = 0.13). These end product characteristics could positively impact the physical properties of soils, increasing porosity and Water retention capacity (WRC). WRC is the amount of water held in soil pores after gravity loss for a specified time. The NTC 5167 recommends values higher than 100%. All treatments had WRC values above 200%, treatments B and C with statistically significant differences from treatment A (p = 0.036) and higher values. The high WRC values found in this research are associated with SW that increases the porosity and density of products.
The Cation Exchange Capacity (CEC) indicates the end product ability to sustain the exchange of cations such as potassium (K), calcium (Ca), magnesium (Mg), and sodium (Na) with surfaces negatively charged (Hemidat et al., 2018; Soto-Paz et al., 2019). This parameter tends to increase through the process due to the mineralization of organic matter (Waqas et al., 2018). The NTC 5167 set a minimum value for CEC of 30 meq/100 g. Thus, all treatments fulfilled this requirement, although treatment C had the lowest value (44.1 ± 1.5) and was statistically different (p = 0.019) compared to treatments A and B. End products with this CEC could stimulate the biological activity due to the exchange of bases with the soil. On the other hand, EC in end products from treatments A and B was around 4 mS/cm. Our results were higher (4.3 mS/cm) compared to the values recommended by the NCH 2880, Bernal et al. (2017) for agricultural use ( CE < 3.0 dS/cm), and Cesaro et al. (2015) in the European context, suggesting that end products could add a potential degree of salinity to the soil. On the other hand, treatment C had the lowest CEC values from all treatments, possibly due to the absence of CM.
The Ash content was constant during composting, although, due to the loss of mass and water, it increased concentration (Bernal et al., 2017). The end products from all treatments had an Ash concentration lower to 60%, the maximum accepted value according to NTC 5167. The higher ash content was found in treatment C, which can be associated with mineral or inorganic material from the soil added to the SO waste.
Regarding TOC, all treatments had a concentration over 15%, minimum value recommended by the NTC 5167 and higher than that reported by Rizzo et al. (2013) in the composting of CM and by Soto-Paz et al. (2019) in the composting of Bw with different co-substrates. There were no statistically significant differences between treatments (p = 0.075), which could increase the organic matter content in degraded soils (Lasaridi et al., 2006; Hargreaves et al., 2008). Regarding TN, treatments A and B fulfilled NTC 5167 and NCH2880 (TN > 1%) and lacked statistically significant differences (p = 0.78). These results show a higher concentration of TN at the end of the process than in other research addressing composting of flowers and food waste with ashes. On the other hand, Treatment C had lower concentrations of TN among treatments. Thus, the operational conditions in this treatment were unfavorable for the composting process. In other conditions, introducing a bulking agent, an amendment, or both, allowed improving the media porosity, C/N ratio, and the aeration of the matrix; this could help keep ammonia in equilibrium between the water and gas phase.
The C/N ratio has been extensively used to indicate maturity and stability during composting (Bernal et al., 2017). However, Bernal et al. (2017) indicate that this relation is closer to substrates than maturity. Some authors propose admissible values for the C/N ratio of the end product. For instance, the standards from the Hong Kong Organic Resource Centre (2005): < 25. There were no statistically significant differences for C/N (p = 0.16) between treatments A and B, and fulfilled this requirement. In contrast, Treatment C had a slightly high value (57.7 ± 2.9) that may be because it was the only treatment with a higher quantity of sawdust, a carbon-rich substrate.
A fraction of the Total P, Ca, and Mg is present in the end product and available for the plant. Essentially, a total K in compost is available in the end product (Hargreaves et al., 2008). According to the NTC 5167, TP and TK content must be higher than 1% for organic products. The results obtained show that the treatments did not achieve the quality criteria regarding TP. Thus, end product quality has limitations and does not comply with NTC 5167 and NCH 2880 (Lasaridi et al., 2006). Treatments A and B were statistically different regards treatment C (p = 0.027).
In contrast, for TK, treatments A and B had concentrations above 1%, without statistical differences between treatments (p = 0.81), which increases the agricultural value of these products. In the case of treatment C, TK concentration was below 1%, highlighting the need to identify alternative sources of waste that contain these nutrients to improve end product quality. Regarding the presence of oligo-elements, all treatments had Ca, Mg, Na and Zn, which can be used for the microorganisms in the soil and stimulate assimilation of macronutrients and their availability for the plants (Lasaridi et al., 2006; Hargreaves et al., 2008).
The Fertility Index (FI) values were above 4.2 in Treatments A and B, making them more appropriate for use in the soil (Saha et al., 2010). In the case of treatment C, the FI was 2.6, which indicates the need to prepare raw materials with other elements to improve end-product quality. This result is associated with the limited concentration of TN and TP that reduces its soil applicability for agricultural purposes. However, this product could be used as landfill cover material.
Stability and maturity: The end products from all treatments had germination indexes (GI) associated with products considered mature (non-phytotoxic) and with high fertilization potential (Fig. 4). Treatment C had the best GI, above 100%, which according to Komilis y Tziouvaras (2009), indicates that these products increase plant growth rather than impair it. This behavior is due to the low EC values (< 1%), and consequently, less availability of salts. On the other hand, the self-heating test evidenced that all treatments had a stability degree of IV, indicating that end products were stable.
Figure 4 here