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Table 2 Consumption and production of major chemicals and products during the willow harvesting, hot water extraction, fermentation and ethanol recovery

From: Life cycle greenhouse gas emissions of ethanol produced via fermentation of sugars derived from shrub willow (Salix ssp.) hot water extraction in the Northeast United States

 

Unit

Previous land use

Cropland

Grassland

Harvesting

 Harvester fuel consumption (leaf-on)

L/Mg

5.7

6.0

 Harvester fuel consumption (leaf-off)

L/Mg

3.1

3.2

 Harvested biomass (leaf on)

103 Mg/year

315

315

 Harvested biomass (leaf off)

103 Mg/year

269

269

  

Energy source

Biomass

Natural gas

HWE Input

 Wood chips

Mg/day

700

700

 Sulfuric acid

Mg/day

3.28

3.28

 Hydrochloric acid

Mg/day

0.41

0.41

 Calcium hydroxide

Mg/day

3.06

3.06

 Sodium hydroxide

Mg/day

0.04

0.04

 Formic acid

Mg/day

2.07

2.07

 Flocculant

Mg/day

0.15

0.15

 Membrane (8 × 40″)

unit/year

1527

1527

 Water

103 Mg/day

4.2

4.2

 Energy requirement (extraction)

GJ/day

501

506

 Energy requirement (extract processing)

GJ/day

750

758

HWE

Output

 HWE processed wood chips

Mg/day

393a

543a

 Sugars

Mg/day

97.4

97.4

 Acetic acid

Mg/day

17.3

17.3

 Phenolic resins

Mg/day

28.0

28.0

 Methanol

Mg/day

5.04

5.04

 Furfural

Mg/day

3.61

3.61

Fermentation and recovery

Input

 Energy requirement (fermentation)

GJ/day

23.0

23.0

 Energy requirement (distillation)

GJ/day

304

304

 Initial cell concentration (10% v)

g/g sugar

0.044

0.044

Fermentation and recovery

Output

 Ethanol

Mg/day

39.6

39.6

Waste treatment

Output

 Waste water

Mg/day

1760

1760

 Ash

Mg/day

1.86

0.00

Excess electricity

 Electricity

GJ/day

134

146

  1. aFewer HWE chips leave the system boundary under the biomass scenario than natural gas, because a fraction of the HWE chips is combusted in a combined heat and power (CHP) system to meet the heat and electricity requirement of the biorefinery