Hydrothermal Liquefaction: Effect of Various Waste ...

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Properties of water. Hydrothermal liquefaction (HTL). Manure and sludge as liquid media for HTL. Biocrude yield using two different solvents. Physical ...
Hydrothermal Liquefaction: Effect of Various Waste Streams as Reaction Medium M. Toufiq Reza, PhD With co-authors Akbar Saba and Chuck Coronella of University of Nevada Reno Reza Shekarriz of HydroTORR LLC. AIChE Annual Conference, 11 November 2015, Salt Lake City, UT

University of Nevada, Reno

 Land grant university  UNR has ~ 20,000 students  Tier 1 university- wide range of academic disciplines 2

Outline  Properties of water  Hydrothermal liquefaction (HTL)  Manure and sludge as liquid media for HTL  Biocrude yield using two different solvents  Physical properties of biocrude  Chemical constituents of biocrude  Conclusions

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Subcritical water

Dielectric constant  Non-polar solvent Ionic product  more ions

Physical properties of water with temperature, at 24 MPa [1]

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Carbonization

Hydrothermal Treatment

Phase diagram of water [2,3]

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Hydrothermal Liquefaction  Hot compressed water (250 – 374 °C)  Short contact time (20-60 min)  High Pressure : vapor pressure of liquid water (5-22 MPa) Gases (mostly CO2) Polar compounds (acids, phenols etc)

Biomass Water

Biocrude

250 – 374 ˚C Solid char

Loblolly pine

Water Hydrothermal liquefaction process

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Why HTL? 1. Wet process 2. Possible to avoid expensive pre-drying 3. Accepts numerous biomass types 4. Can converts waste to energy 5. Non-catalytic process 6. Straightforward process 8. Biocrude can be upgraded to liquid fuels

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The challenge  HTL requires water; usual practice 10-15% solid  Modern dairies produce a lot of manure (up to 50 kg per

cow per day)

 More than 20 million ton/year (dry basis) in the U.S.  Moisture > 90% and >15% ash

 7 MT dry sewage sludge were produced in the US in 2014  Contains >85% moisture and >25% ash  Mostly landfilled and/or incinerated

 Synergetic effect- as both manure and sludge contains

carbons  Can we use manure and sewage sludge as water source of HTL? 8

Objectives  Perform HTL of loblolly pine using dairy manure and sewage

sludge as moisture source  Monitoring biocrude yield by polar and non-polar solvents  Physical characterization of biocrudes  Density  Viscosity

 Chemical characterization of biocrudes  CHON elemental analysis  GC/MS  FTIR 9

Properties of feedstocks Origin Loblolly pine Dairy manure Sewage sludge

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Southern Alabama, 2013 UNR experimen tal station TMWRF Local WWT plant

Moisture (%) 5-8

pH

Ash (%)

N/D

0.2-0.5

HHV daf (MJ kg-1) 19.5-20.0

85-90

5.0-5.5

20-25%

18-19

85-90

7.8-8.0

25-30%

18-20

Experimental matrix Sample Loblolly pine Manure Sludge Manure/LP Sludge/LP LP Manure Sludge Manure/LP Sludge/LP 11

T (°C)

Solvent

250

275

300

Acetone

250

275

300

Cyclohexane

HTL Procedure 2L Parr reactor

• 68 g loblolly pine • 440 g manure/sludge • 30 min reaction at HTL temperature

Liquid-liquid separation

• Filter solid/add solvent • 300 ml cyclohexane/acetone • Acetone used on dry solids only

Rotary evaporation

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• Separate solvents from biocrude

Results

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Biocrude Yield (Acetone extracted)

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Biocrude Yield (Cy.Hexane extracted)

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Biocrude Yield (per g of LP basis)

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Acetone extracted biocrude yield at 300 °C

Cyclohexane extracted biocrude yield at 300 °C

Energy content (Acetone Ext. Biocrudes)

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Energy content (Acetone vs Cy. Hexane)

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HHV of sludge biocrude

HHV of sludge/LP biocrude

Density

2 ml Pycnometer

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Elemental Analysis C

H

85

O

80

20

75 15

70

10

65 60

5

55

0

50

LP 20

Man

Sl

Man/LP Sl/LP

Carbon concentration (%)

O, H concentration (%)

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Viscosity (Sl/LP biocrudes) 25 °C

1000 100

100

10 1 0.1

50 °C

1000

1

21

10000

Complex viscosity (Pa-s)

Complex viscosity (Pa-s)

10000

2 LP-acetone LP-Sludge cyclohexane LP-Sludge acetone Sludge cyclohexane

10

1

0.1

0.01

1

2

Viscosity (Man/LP biocrudes)

Complex viscosity (Pa-s)

10000

50 °C

1000

100

10

1 1 22

2

Viscosity

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Viscoelastic properties of biocrudes (T = 300 °C)

Rheometer

FTIR: LP

Aliphatic ‐CH

'LP-250-Acetone' 'LP-275-acetone' 'LP-300-Acetone'

–C=O ring –C‐C 3100 24

2600

2100

1600

1100

600

FTIR: Manure/LP

–C=O ring –C‐C Aliphatic ‐CH

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C=C

FTIR: Sludge/LP

–CH –C=O

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–C‐C ring

–C‐O stretch

GCMS: Acetone Extract

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GCMS: Cyclohexane Extract

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Remaining steps  HTL temperature T>300 °C  Optimization  Reaction mechanism  Upgrade biocrude to jet fuel  Life cycle analysis  TEA

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Conclusions • Dairy manure and sewage sludge have synergetic effect on HTL • Biocrude yield was as much as 30% for both acetone and • • • • •

cyclohexane solvent in basis of LP only Cyclohexane is more effective for Sludge/LP than Man/LP C content reached >80%, O< 5% and HHV > 40 MJ kg-1 Densities: Cyclohexane 1000 kg m-3 Sludge/LP biocrude complex viscosity