Cost and life cycle assessment of biomass densification

Sultana et al. (2010) performed a techno-economic analysis and developed a model for a plant that can produce agricultural straw (barley, oat and wheat) pellets for 30 years. They have included the cost of obtaining the straw, transporting straw to the pellet plant, and producing pellets. Costs incurred by the plant for the production of pellets included capital cost, energy cost, labor cost, and consumable cost. The biomass procurement area was determined to estimate the transportation cost. The scale factors for all the equipment related to pellet production were determined based on the data of previous studies (Sultana et al., 2010). To develop the model, minimum, average and maximum yields of wheat, barley and oats straw in Western Canada were considered. They have determined that the cost of pellets does not change much for capacities over 70,000 tonnes per year (cost of production per tonne is $170.89). Therefore, the optimum size is the same for both average and maximum yield cases. In addition, it was observed that the total cost of pellet production is most sensitive to field cost followed by the transportation cost.

Life cycle assessment (LCA) study was performed on wheat straw production system and densification system in the Canadian Prairies using the LCA modelling software tool SimaPro 7.2 to determine the environmental burdens of manufacturing the wheat straw bale and wheat straw pellet (Li et al., 2011). The factors taken into consideration were greenhouse gas emission, acidification, eutrophication, ozone layer depletion, abiotic depletion, human toxicity, and photochemical oxidation. Li et al. (2011) reported that the production of biomass pellet has higher global warming effect than biomass bale, especially in CO2 and CH4 emissions from fossil fuel consumption, which is very high in densification system due to machinery usage. It was also reported that the production of wheat straw pellet has higher environmental impact on acidification, eutrophication, human toxicity and other categories than biomass bale. The dominant factors determining most environmental impacts in agricultural system are fertilizer use and production, while machinery use, manufacturing and energy consumption are main contributors to greenhouse gas emission and other environmental burdens in the densification system (Li et al., 2011).

Agricultural

Biomass

Hammer Mill Screen

Size (mm)

Pellet Density (kg/ m3)

Pellet Bulk Density (kg/m3)

Durability

(%)

Throughput

(kg/h)

Specific

Energy

(MJ/t)

Barley Straw

1.6 (100% NT)

1158±109*t£ aD

665+01Ф aD

91+00Ф aD

4.88

293

0.8 (100% NT)

1174+46 aD

700±07 bD

93±01 bD

4.21

353

0.8 (75% NT + 25% SE)

1184±63 aD

714±02 cD

87±01 cD

3.46

301

Canola Straw

1.6 (100% NT)

1023±85 aE

629±01 aE

90+01 aD

3.86

385

0.8 (100% NT)

1204±43 bDE

720±04 bE

95±00 bE

3.63

440

0.8 (75% NT + 25% SE)

1144±50 cD

641±01 cE

82±00 cE

5.51

265

Oat Straw

1.6 (100% NT)

1140±63 abD

631±03 aE

89+01 aE

4.48

340

0.8 (100% NT)

1188±78 aDE

649±02 bF

93±00 bD

3.81

344

0.8 (75% NT + 25% SE)

1071±101 bE

676±06 cF

89±01 aF

4.03

335

Wheat Straw

1.6 (100% NT)

1163±57 aD

673±02 aF

94+01 aF

5.44

381

0.8 (100% NT)

1278±136 bE

721±04 bE

95±01 bE

3.81

297

0.8 (75% NT + 25% SE)

1213±88 abD

722±04 bG

95+00 cG

4.08

342

NT — Non-treated Straw Samples; SE — Steam Exploded Straw Samples; *10 replicates; ф3 replicates; t 95% confidence interval; £ Student-Neuman-Keuls test at 5% level of significance for same sample biomass at various hammer mill screen sizes (a, b and c); at same hammer mill screen size for different sample biomass (D, E, F and G)

Table 5. Pellet density, durability, throughput and specific energy data for non-treated and steam exploded barley canola, oat and wheat straw at 17.5% moisture content (wb) and 10% flaxseed oil content

Treatment

Hammer Mill Screen Size (mm)

Chopping

Biomass

Specific Energy (MJ/t)

Grinding Pilot-Scale Biomass Pelleting

Total£

HHV

(MJ/t)

Net Energy Y (MJ/t)

Barley

NT*

1.6

11.3

90.4

293

924

16400

15476

NT

0.8

11.3

206.6

353

1100

16400

15300

75% NT + 25%

0.8

11.3

189.3

301

1030

16650

15620

SE*

Canola

NT

1.6

7.1

128.5

385

987

16700

15713

NT

0.8

7.1

363.3

440

1277

16700

15423

75% NT + 25% SE

0.8

7.1

341.6

265

1080

17100

16020

Oat

NT

1.6

9.9

149.5

340

1029

16400

15371

NT

0.8

9.9

253.6

344

1137

16400

15263

75% NT + 25% SE

0.8

9.9

245.2

335

1120

16750

15630

Wheat

NT

1.6

8.2

153.3

381

1048

17000

15952

NT

0.8

8.2

382.7

297

1194

17000

15806

75% NT + 25% SE

0.8

8.2

332.1

342

1188

17200

16012

*NT — Non-Treated; SE — Steam Exploded

£ Total Specific Energy = Specific Energy (Chopping Biomass + Operating Chopper + Grinding Biomass + Operating Hammer Mill + Pilot-Scale Pelleting)

YNet Energy = HHV — Total

Table 6. Overall specific energy analysis to show net energy available for production of biofuels after postharvest processing and densification of agricultural straw.