Insights about the Choice of Pig Manure Processing System in Three Italian Regions: Piemonte, Friuli Venezia Giulia, and Veneto
Abstract
:1. Introduction
2. Materials and Methods
2.1. The Case Study
2.2. Sampling
2.3. The Survey
2.4. Data Analysis
3. Results
3.1. Descriptive Statistics
3.2. Manure Management Systems and Motivation
- The minimization of treatment costs;
- The minimization of spreading costs;
- Maximization of the agronomical value of the nutrients contained in the slurry;
- The minimization of GHG emissions;
- The valorization of by-products;
- The minimization of acidic gas emissions.
3.3. Perception of Critical Issues and Upgradeability
4. Discussion
4.1. Adoption Drivers of Different Processing Techniques
4.2. Adoption Dirvers from a Geographical Perspective
- One out of 22 was interested in adopting different spreading systems (umbilical system);
- Two out of 22 had no idea about what innovation could be useful and asked for technical support in order to define the most suitable improvement;
- One out of 22 was interested in reducing N in the separated liquid phase (this is the case of the farm already adopting Ad-Cstr + Centrifuge screw separation + Zeolite filter);
- One out of 22 was interested in thermos-valorizing the treatment and producing biogas;
- Two out of 22 were interested in implementing Ad-Cstr;
- One out of 22 was interested in adopting an oxygenation system for storage.
5. Conclusions
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Acknowledgments
Conflicts of Interest
Appendix A
Processing Technology | Aim | Investment Cost (€/m3) | Treatment Cost (€/m3) |
---|---|---|---|
Mechanical solid–liquid separation of slurry by a screw press, decanter centrifuge, coagulation–flocculation, sieve-drum filters, filter press, air flotation, natural settling | Separation and concentration of the solid and liquid fractions of slurry | Coagulation–flocculation: Investment cost, basic price, €: 50,000; investment cost, variable price, € per tonne: 0.65 | ~0.80 €/tonne input slurry [43]. |
Screw press: Investment cost, basic price, €: 28,000; Investment cost, variable price, € per tonne: 0.36 | Treatment cost between 0.5 and 0.9 €/m3 of input [44]. | ||
Decanter centrifuge: Investment cost, basic price, €: 110,000; investment cost, variable price, € per tonne: 1.42 | Treatment cost between 0.6 and 2.3 €/m3 of input manure [44]. | ||
Air flotation (coupled with flocculation): no data. | No valid data available. However, a plant in Holland (Kumac Mineralen), which used flotation in addition to flocculation, drum belt separation, reverse osmosis, and demineralization, claimed the operational costs for all processes were at a level of 5 €/m3 slurry. | ||
Drum-filters: Basic investment of approx. 25,000 euro at a capacity of 2–3 m3 slurry/hour. | Approx. 0.35 euro/m3 slurry | ||
Natural settling: 17,000 € for a thickener volume of 350 m3 [44]. | Irrelevant | ||
Sieves (static or vibrant): Investment cost, basic price, 3500–8000 € (sieve), 15,000 € (vibrant) according to [43]. Investment cost, variable price, € per tonne: 0.19 | According to [45], the operational costs comprise 1.31 kWh/tonne electricity consumption. | ||
Filter press: Investment cost, basic price, €: 75,000; investment cost, variable price, € per tonne: 0.97 | Operational costs, € per tonne: 1.5. Operational costs, explanation: 1.5 €/tonne of input manure (band filter) [43]. | ||
Aeration of liquid manure/biological treatment: Aerobic digestion, nitrification denitrification | Biological decomposition of organic matter. Removal of ammoniacal nitrogen as N2 gas | Nitro-Denitr. Investment cost: 240,000–300,000 € (plant treating 15,000 m3 pig slurry/year); 700,000–1,200,000 € (plant treating 50,000 m3 pig slurry/year) | Operational costs, explanation: Costs are dependent on the composition of the manure to be treated. 1.5–3.0 €/tonne considering exclusively N removal treatment. 2.5–5.2 €/tonne considering previous separation S/L, and the later treatment of the solid fraction by composting. |
Composting of solid manure: Composting, co-composting of poultry manure with green residues, composting with a biological inoculum | Obtain a stable product with a low moisture content and retaining most of the initial nutrients, free of pathogens | Equipment:
| As guidance: 20 €/tonne |
Anaerobic treatment | Production of biogas. Mineralization and stabilization of organic matter | Investment cost-basic price, €: 750,000 [43]; investment cost-variable price, € per tonne: 50 | Operational costs, € per tonne: 2.1. Operational costs, explanation: The operational costs indicated here include costs such as internal electricity consumption, labor, and insurance. In addition to this, it would be expected that maintenance costs of the plant represent 2–2.5% of the investment cost. Costs for transport of livestock manure and other in and out of the biogas plant is as indicated under investment costs estimated by [46], with a value of 7–4.7 €/m3. |
Anaerobic lagoon system | Combined slurry stabilization, separation, and storage | Investment cost, variable price, € per cow: 580 [47] | Operating cost, € per milk tonne: 1.85 (author’s computation based on [47]) |
Evaporation and drying of manure. Slurry and wet manure belt dryer | Increase nutrient and organic matter concentration. Reduced volume for easier and cheaper transport. | Investment cost-basic price, €: 250,000 [48]; nvestment cost, variable price, € per tonne: 2.1 (author’s computation based on [48]) | Operational costs, € per tonne: 2.5 (author’s computation based on [48]) |
Slurry acidification | Reduction of ammonia emissions by lowering the pH of manure, with consequent ammonium (NH4-N) retention in the manure | There is a basic investment in the range of 25,000–100,000 € at a farm level (including storage tanks, pumps, and controllers), but dependent on the farm size and types of stables and other local parameters, such as the implementation of the sole spreading or storage plus spreading. | Operational costs, explanation: The total additional cost is app. € 20 per ha for use of acidification during spreading. This extra cost includes depreciation of the investment. The aggregate for slurry acidification in storage tanks is considerably cheaper than the required investments in acidification during spreading, but it has to be taken into consideration that slurry acidification in storage tanks due to foaming of the slurry during the process requires a freeboard in the tanks of 0.8–1 m, wherefore their capacity cannot be fully utilized. There are no noteworthy maintenance requirements of the acidification technology. |
Ammonia stripping | Removal of ammonia through volatilization from a liquid phase, with subsequent recovery in an acidic solution as ammonium salt or by condensation. Often coupled with AD and biogas production [48]. | Investment cost: For an industrial plant projected in Catalonia for treating 10 m3/h of digested pig slurry (stripping including storage tanks and condensers), the investment cost was estimated to be 0.4–0.5 M€. For the Ihan plant located in Slovenia, treating 15 m3/h, the estimated investment cost of the stripping column was 0.25 M€. | Operational costs, explanation: Reagent cost: 0.66 €/m3 for NaOH/0.21 €/m3 for H2SO4 2.5–4.5 €/kg of stripped nitrogen (only for the stripping column) [49]. At least an equivalent range of values should be considered for the absorption step. |
Manure additives | Facilitate handling and management of manure. Stabilization of manure and reduction of the pathogen contents |
N ID | Region (NUTS 2) | Province (NUTS 3) | Municipality | Type of Pig Breeding |
---|---|---|---|---|
1 | PIEMONTE | CN | VILLAFALLETTO | Farrow-to-finish |
2 | PIEMONTE | CN | PEVERAGNO | Feeder-to-finish |
3 | PIEMONTE | CN | SCARNAFIGI | Feeder-to-finish |
4 | PIEMONTE | TO | CARMAGNOLA | Feeder-to-finish |
5 | PIEMONTE | TO | RIVA PRESSO CHIERI | Farrow-to-finish |
6 | PIEMONTE | CN | RACCONIGI | Farrow-to-finish |
7 | PIEMONTE | TO | CARIGNANO | Feeder-to-finish |
8 | PIEMONTE | TO | RIVA PRESSO CHIERI | Farrow-to-finish |
9 | PIEMONTE | TO | RIVA PRESSO CHIERI | Farrow-to-feeder |
10 | PIEMONTE | TO | RIVA PRESSO CHIERI | Feeder-to-finish |
11 | PIEMONTE | NO | NOVARA-FR.OLENGO | Feeder-to-finish |
12 | PIEMONTE | TO | CHIERI | Feeder-to-finish |
13 | PIEMONTE | TO | RIVA PRESSO CHIERI | Feeder-to-finish |
14 | PIEMONTE | TO | CAMBIANO | Feeder-to-finish |
15 | FRIULI VENEZIA GIULIA | PN | SAN MARTINO AL TAGLIAMENTO | Not specified |
16 | FRIULI VENEZIA GIULIA | PN | SPILIMBERGO | Not specified |
17 | FRIULI VENEZIA GIULIA | PN | SPILIMBERGO | Farrow-to-finish |
18 | FRIULI VENEZIA GIULIA | PN | VIVARO | Not specified |
19 | FRIULI VENEZIA GIULIA | PN | CAVASSO NUOVO | Not specified |
20 | FRIULI VENEZIA GIULIA | PN | MANIAGO | Feeder-to-finish |
21 | FRIULI VENEZIA GIULIA | PN | VALVASONE | Farrow-to-feeder |
22 | FRIULI VENEZIA GIULIA | UD | RONCHIS | Farrow-to-finish |
23 | FRIULI VENEZIA GIULIA | UD | RIVIGNANO TEOR | Not specified |
24 | FRIULI VENEZIA GIULIA | UD | FRAFOREANO DI RONCHIS | Farrow-to-finish |
25 | FRIULI VENEZIA GIULIA | PN | PORCIA | Farrow-to-feeder |
26 | FRIULI VENEZIA GIULIA | PN | SACILE | Not specified |
27 | VENETO | VN | SALIZZOLE (VN) | Feeder-to-finish |
28 | VENETO | PD | PONSO (PD) | Farrow-to-feeder |
29 | VENETO | PD | STANGHELLA (PD) | Feeder-to-finish |
30 | VENETO | TV | ZERO BRANCO (TV) | Farrow-to-feeder |
31 | VENETO | TV | SAN BIAGIO DI CALLALTA TV | Farrow-to-feeder |
32 | VENETO | VR | NOGAROLE ROCCA (VR) | Feeder-to-finish |
33 | VENETO | PD | SANT’URBANO (PD) | Farrow-to-feeder |
34 | VENETO | TV | SAN BIAGIO DI CALLALTA, TV | Farrow-to-feeder |
35 | VENETO | VI | ROSÀ (VI) | Farrow-to-finish |
36 | VENETO | VE | CAMPAGNA LUPIA | Farrow-to-finish |
37 | VENETO | PD | MASSANZAGO | Feeder-to-finish |
38 | VENETO | PD | MASSANZAGO | Feeder-to-finish |
39 | VENETO | PD | CAMPOSANPIERO | Farrow-to-finish |
40 | VENETO | PD | TOMBOLO | Feeder-to-finish |
Average Manure Volume (Produced, Cubic Meters) | St. Dev. | Average Manure Volume (Stored, Cubic Meters) | St. Dev. | Variation % (between Volume Produced and Stored) | |
---|---|---|---|---|---|
FVG | 11,258.3 | 10,061.7 | 12,351.6 | 11,563.0 | 8.9% |
P | 14,366.6 | 7373.2 | 15,029.3 | 7850.5 | 4.4% |
V | 13,609.0 | 7434.6 | 14,363.9 | 8125.5 | 5.3% |
Whole sample | 13,169.0 | 8173.6 | 13,993.1 | 9029.2 | 5.9% |
Average, Available Land (ha) | St. Dev of Available Land (ha) | Average, Owned Land (% of the Total Available Land) | St. Dev of Owned Land (% of the Total Available Land) | Average, Zones Vulnerable to N-leaching (% of the Total Available Land) | St. Dev of Zones Vulnerable to N-Leaching (% of the Total Available Land) | |
---|---|---|---|---|---|---|
FVG | 170.91 | 122.11 | 0.25 | 0.30 | 0.30 | 0.45 |
P | 189.98 | 85.12 | 0.44 | 0.21 | 0.62 | 0.36 |
V | 203.37 | 113.10 | 0.31 | 0.35 | 0.61 | 0.41 |
Whole sample | 188.95 | 105.16 | 0.36 | 0.29 | 0.52 | 0.42 |
Trees and Vineyards | Grain Legumes | Cereal-Crops | Oil and other Crops | Vegetables | Forage | Pasture and Grassland | |
---|---|---|---|---|---|---|---|
FVG | 6.5% | 18.5% | 66.8% | 2.2% | 0.3% | 5.0% | 0.6% |
P | 1.2% | 6.0% | 87.2% | 0.4% | 0.0% | 1.2% | 4.0% |
V | 7.1% | 15.9% | 55.0% | 0.8% | 2.0% | 18.1% | 1.0% |
Total | 4.9% | 13.2% | 69.8% | 1.1% | 0.8% | 8.3% | 1.9% |
Adopted Technique | Minimization of Treatment Costs | Minimization of Spreading Costs | Minimization of GHG Emissions | Minimization of Acidic Gas Emissions | Maximization of the Agronomical Value of the Nutrients Contained in the Slurry | Valorization of by-Products |
---|---|---|---|---|---|---|
Tanks or Stalls storage | 3.7 | 2.8 | 2.1 | 1.2 | 2.1 | 1.7 |
Centrifuge separation | 2.0 | 5.0 | 4.0 | 3.0 | 1.0 | 1.0 |
Ad-Cstr | 3.0 | 1.0 | 5.0 | 1.0 | 4.0 | 2.0 |
Centrifuge separation + Ad-Cstr | 1.0 | 1.0 | 1.0 | 1.0 | 2.3 | 3.7 |
BNR-SBR | 2.0 | 5.0 | 4.0 | 3.0 | 1.0 | 1.0 |
BNR-Continuous | 1.0 | 1.0 | 1.0 | 1.0 | 1.0 | 1.0 |
Centrifugal separation + Ad-Cstr + BNR-SBR | 4.0 | 5.0 | 1.0 | 1.0 | 3.0 | 2.0 |
Adopted Technique | FVG | P | V * | Whole Sample |
---|---|---|---|---|
Tanks or Stalls storage | 100.0% | 71.4% | 78.6% | 82.5% |
Screw press separation | 0.0% | 0.0% | 7.1% | 2.5% |
Ad-Cstr | 0.0% | 0.0% | 7.1% | 2.5% |
Screw press separation + Ad-Cstr | 0.0% | 21.4% | 0.0% | 7.5% |
NBR-SBR | 0.0% | 0.0% | 7.1% | 2.5% |
NBR-Continuous | 0.0% | 7.1% | 0.0% | 2.5% |
Centrifugal separation + Ad-Cstr + NBR-SBR | 0.0% | 0.0% | 7.1% | 2.5% |
High Distance of Available Lands | High Management Costs | High Investment Cost | Low Availability of Information on Upgrades | Total N° of Farms | High Distance of Available Lands | High Management Costs | High Investment Cost | Low Availability of Information on Upgrades | |
---|---|---|---|---|---|---|---|---|---|
FVG | 5.0 | 8.0 | 10.0 | 5.0 | 12.0 | 41.7% | 66.7% | 83.3% | 41.7% |
P | 7.0 | 2.0 | 3.0 | 3.0 | 14.0 | 50.0% | 14.3% | 21.4% | 21.4% |
V | 3.0 | 4.0 | 7.0 | 1.0 | 14.0 | 21.4% | 28.6% | 50.0% | 7.1% |
Whole sample | 15.0 | 14.0 | 20.0 | 9.0 | 40.0 | 37.5% | 35.0% | 50.0% | 22.5% |
% of ZVN on Total Available Land | Injection | Broadcasting with Incorporation | Broadcasting, No Incorporation | Total % | Total |
---|---|---|---|---|---|
Less than 9% | 7.7% | 69.2% | 23.1% | 100.0% | 13 |
10–49% | 14.3% | 57.1% | 28.6% | 100.0% | 7 |
More than 50% | 20.0% | 65.0% | 15.0% | 100.0% | 20 |
Whole sample | 0.15 | 0.65 | 0.2 | 1 | 40 |
What treatment is actually adopted by the farms saying “no/yes” to upgradeability? | Upgradeability | No Processing-Only Storage | Screw Press Separation | Ad-Cstr | Screw Press Separation + Ad-Cstr | BNR-SBR | BNR-Continuous | Centrifugal Separation + AD-Cstr+ NBR-SBR | Total |
NO | 17 | 2 | 1 | 18 | |||||
YES | 18 | 1 | 1 | 1 | 1 | 1 | 22 | ||
Total | 35 | 1 | 1 | 3 | 1 | 1 | 1 | 40 |
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Question Topic | N° and Type of Question |
---|---|
| 6 open questions |
| 8 open questions (for each plot) |
| 6 open questions (for each building) |
| 5 open questions (for each structure) |
| 17 alternatives in multiple checkboxes |
| open question (up to 3) |
| open question (up to 3) |
| 6 alternatives assessed through personal 1 to 5 scoring |
| 4 alternatives in multiple checkboxes |
| y/n question |
| open question |
| y/n question |
| 6 open questions (for each plot) |
| y/n question |
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De Marinis, P.; Ferrari, O.; Allisiardi, E.; De Mattia, C.; Caliandro, G.; Dinuccio, E.; Borin, M.; Ceccon, P.; Sali, G.; Provolo, G. Insights about the Choice of Pig Manure Processing System in Three Italian Regions: Piemonte, Friuli Venezia Giulia, and Veneto. Sustainability 2021, 13, 787. https://doi.org/10.3390/su13020787
De Marinis P, Ferrari O, Allisiardi E, De Mattia C, Caliandro G, Dinuccio E, Borin M, Ceccon P, Sali G, Provolo G. Insights about the Choice of Pig Manure Processing System in Three Italian Regions: Piemonte, Friuli Venezia Giulia, and Veneto. Sustainability. 2021; 13(2):787. https://doi.org/10.3390/su13020787
Chicago/Turabian StyleDe Marinis, Pietro, Omar Ferrari, Erica Allisiardi, Chiara De Mattia, Giuliana Caliandro, Elio Dinuccio, Maurizio Borin, Paolo Ceccon, Guido Sali, and Giorgio Provolo. 2021. "Insights about the Choice of Pig Manure Processing System in Three Italian Regions: Piemonte, Friuli Venezia Giulia, and Veneto" Sustainability 13, no. 2: 787. https://doi.org/10.3390/su13020787
APA StyleDe Marinis, P., Ferrari, O., Allisiardi, E., De Mattia, C., Caliandro, G., Dinuccio, E., Borin, M., Ceccon, P., Sali, G., & Provolo, G. (2021). Insights about the Choice of Pig Manure Processing System in Three Italian Regions: Piemonte, Friuli Venezia Giulia, and Veneto. Sustainability, 13(2), 787. https://doi.org/10.3390/su13020787