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Renewable Hydrocarbon Oils and Chemicals from Solar Energy and Carbon Dioxide Pradeep Munasinghe*, Shimin Kang and Jian Yu ( [email protected] ), Hawaii Natural Energy Institute University of Hawaii at Manoa, 1680 East-West Rd. Honolulu, HI 96822, USA Introduction: A novel technology is being developed to produce hydrocarbon oil and chemicals (C7-C16) from CO 2 and solar energy. The process consists of water hydrolysis with solar electricity, hydrogen-based CO 2 fixation by an autolithotrophic bacterium under dark conditions, and thermal catalytic conversion of the cell mass into hydrocarbon oil. Aromatics are the major compounds in the oil. High performance transportation fuels can therefore be produced, by refining the renewable oil. Result 1: CO 2 assimilation and cell growth on flue gas (CO 2 :H 2 :O 2 :N 2 =9:39:13:39) and PHB formation with nitrogen nutrient depletion: high cell density of 22 g/L with 60% PHB in 160 hrs. Method: The process consists of a photovoltaic assembly, a water electrolyzer, a dark fermenter in which autotrophic hydrogen-oxidizing bacterium assimilates CO 2 with H 2 and O 2 . The biomass is converted into renewable oil and chemicals in a thermal reactor. Result 2: Maximum yield of 0.7 g Cell mass/ g H 2 Result 3: One-pot conversion of cell mass into hydrocarbon oil in 100% H 3 PO 4, 220 o C, 3 hours with oil yield 20 % of biomass or 40% of PHB. Stoichiometric equation: for the exponential growth of the cells and PHB in autotrophic culture 4.1 CO 2 + 21.4 H 2 + 6.2 O 2 + 0.8 NH 3 C 4.1 H 7.1 N 0.8 + 18.7 H 2 O PHB accumulation: 4 CO 2 + 33 H 2 + 12 O 2 C 4 H 6 O 2 + 30 H 2 O Ref. Tanaka K. et al. (1995) Biotech. Bioeng. 45:268-275 Ref. Kang S. & Yu J.(2014) RSC Adv. 4(28): 14320-14327. Result 4: Composition of PHB oil with GC-MS Chemicals Oxygenate Acyclic alkane Cyclo- alkane Acyclic alkene Cyclo- alkene Benzene Naphthalene Area (%) 7.9 0.6 0.1 0.1 2.0 79.0 10.4 Carbon distribution <C7 C7-C8 C9-C10 C11-C12 C13-C14 C15-C16 >C16 Area (%) ND 0.1 8.2 18.8 52.7 19.2 ND Bacterial cell mass (about 52% of PHB) 220 C, 3 hrs One-pot in H 3 PO 4 CO 2 , propylene Hydrocarbon oil 0 20 40 60 80 0 5 10 15 20 25 0 25 50 75 100 125 150 175 PHB content (wt%) Cell density, RCM (g/L) Time (h) Cell density Residue cell mass PHB content 0 20 40 60 80 0.0 0.2 0.4 0.6 0.8 0 25 50 75 100 125 150 175 Dissolved oxygen (%) Cell yield (g)/ H 2 (g) Time (h) Cell yield Dissolved oxygen Result 5: High performance transportation fuels from PHB oil (light & heavy fractions) Fuels Gasoline PHB oil- Light PHB oil- heavy Ethanol BP ( o C) 40-200 40-250 >250 78 C (wt%) 80.4 83.2 65.5 52.2 H (wt%) 12.3 10.3 8.6 13.0 O (wt%) 6.4 6.3 25.6 34.8 HHV (MJ/kg) 41.8 42.1 34.4 29.7 Acknowledgement: Funds from Office of Naval Research (HEET10, APRISES’11)

Renewable Hydrocarbon Oils and Chemicals from Solar Energy

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Renewable Hydrocarbon Oils and Chemicals from Solar Energy and Carbon Dioxide

Pradeep Munasinghe*, Shimin Kang and Jian Yu ([email protected]), Hawaii Natural Energy InstituteUniversity of Hawaii at Manoa, 1680 East-West Rd. Honolulu, HI 96822, USA

Introduction: A novel technology is beingdeveloped to produce hydrocarbon oil andchemicals (C7-C16) from CO2 and solar energy.The process consists of water hydrolysis withsolar electricity, hydrogen-based CO2 fixationby an autolithotrophic bacterium under darkconditions, and thermal catalytic conversion ofthe cell mass into hydrocarbon oil. Aromaticsare the major compounds in the oil. Highperformance transportation fuels cantherefore be produced, by refining therenewable oil.

Result 1: CO2 assimilation and cell growth on flue gas (CO2:H2:O2:N2 =9:39:13:39) and PHB formation with nitrogen nutrient depletion: high cell density of 22 g/L with 60% PHB in 160 hrs.

Method: The process consists of aphotovoltaic assembly, a water electrolyzer, adark fermenter in which autotrophichydrogen-oxidizing bacterium assimilates CO2

with H2 and O2. The biomass is converted intorenewable oil and chemicals in a thermalreactor.

Result 2: Maximum yield of 0.7 g Cell mass/ g H2

Result 3: One-pot conversion of cell mass intohydrocarbon oil in 100% H3PO4, 220 oC, 3 hourswith oil yield 20 % of biomass or 40% of PHB.

Stoichiometric equation: for the exponentialgrowth of the cells and PHB in autotrophic culture4.1 CO2 + 21.4 H2 + 6.2 O2 + 0.8 NH3

C4.1H7.1N0.8 + 18.7 H2O

PHB accumulation:4 CO2 + 33 H2 + 12 O2 C4H6O2 + 30 H2O

Ref. Tanaka K. et al. (1995) Biotech. Bioeng. 45:268-275

Ref. Kang S. & Yu J.(2014) RSC Adv. 4(28): 14320-14327.

Result 4: Composition of PHB oil with GC-MSChemicals Oxygenate Acyclic

alkane

Cyclo-

alkane

Acyclic

alkene

Cyclo-

alkene

Benzene Naphthalene

Area (%) 7.9 0.6 0.1 0.1 2.0 79.0 10.4

Carbon

distribution

<C7 C7-C8 C9-C10 C11-C12 C13-C14 C15-C16 >C16

Area (%) ND 0.1 8.2 18.8 52.7 19.2 ND

Bacterial cell mass

(about 52% of PHB)

220 C, 3 hrs

One-pot in H3PO4

CO2, propylene

Hydrocarbon oil

0

20

40

60

80

0

5

10

15

20

25

0 25 50 75 100 125 150 175

PH

B c

on

ten

t (w

t%)

Ce

ll d

en

sity

, R

CM

(g

/L)

Time (h)

Cell density

Residue cell mass

PHB content

0

20

40

60

80

0.0

0.2

0.4

0.6

0.8

0 25 50 75 100 125 150 175

Dis

solv

ed

oxy

gen

(%

)

Ce

ll yi

eld

(g)

/ H

2(g

)

Time (h)

Cell yield

Dissolved oxygen

Result 5: High performance transportation fuels from PHB oil (light & heavy fractions)Fuels Gasoline PHB oil-

LightPHB oil-heavy

Ethanol

BP (oC) 40-200 40-250 >250 78

C (wt%) 80.4 83.2 65.5 52.2

H (wt%) 12.3 10.3 8.6 13.0

O (wt%) 6.4 6.3 25.6 34.8

HHV (MJ/kg)

41.8 42.1 34.4 29.7

Acknowledgement: Funds from Office of Naval Research (HEET10, APRISES’11)