Process to produce biodiesel and/or fuel oil

• US 8,969,030 B2
• Filed: 05/02/2008
• Issued: 03/03/2015
• Est. Priority Date: 05/02/2007
• Status: Expired due to Fees

• Current Assignee: Ouro Fino Participacoes E Empreendimentos Ltda.
• Original Assignee: Ouro Fino Participacoes E Empreendimentos Ltda.
• Inventors: Neto, Dolivar Coraucci
• Primary Examiner(s): Weber, Jon P
• Assistant Examiner(s): Kosar, Aaron J
• Application Number:
  US12/521,848
• Publication Number:
  US 20100330615A1
• Time in Patent Office: 2,496 Days
• Field of Search: None
• US Class Current: 435/41
• CPC Class Codes: C10G 2300/1011 Biomass
• CPC Class Codes: C10G 2300/1014 of vegetal origin
• CPC Class Codes: C11B 1/10 by extracting
• CPC Class Codes: C11C 3/003 by esterification of fatty acids with alcohols C11C3/02 takes precedence
• CPC Class Codes: C12N 1/22 Processes using, or culture media containing, cellulose or hydrolysates thereof
• CPC Class Codes: C12P 7/6458 by transesterification, e.g. interesterification, ester interchange, alcoholysis or acidolysis
• CPC Class Codes: C12P 7/649 Biodiesel, i.e. fatty acid alkyl esters
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel
• CPC Class Codes: Y02P 20/10 Process efficiency
• CPC Class Codes: Y02P 30/20 using bio-feedstock

Abstract

The present invention refers to a process to produce biodiesel and/or fuel oil from microbial oilseed and/or algal biomass and/or from sugar cane residues and derivatives. The products according to the present invention are appropriate for direct use in motors and to generate energy or steam. The integrated process of the present invention comprises the use, as raw materials, of microbial oil-producing biomass obtained from sugar cane residues and derivatives, which is integrated with algal biomass and/or glycerol and are processed by steps of production of oil-producing microbial biomass from filamentous fungi and/or yeasts, steps of simultaneous production of algal biomass by fully using residues, CO₂ and residual broth of said production of microbial biomass, as well as steps of extraction and transesterification of lipids contained in the biomass, with reuse of the residual glycerol thus produced. The process as disclosed deals with innovative and ecologically sustainable technology, not generating any kind of residue, also providing for the advantage of releasing considerable volumes of oxygen into the atmosphere.

Claims

1. A process for producing biodiesel and/or fuel oil, comprising the steps of:

(a) cultivating oil-producing microbial biomass under conditions sufficient for oil accumulation thereof using residues of sugar cane as a carbon source, wherein the microbe is a yeast or fungus;

(b) obtaining a liquid effluent resulting from the cultivating of step (a) and in the obtained liquid effluent cultivating oil-producing algal biomass under conditions sufficient for oil accumulation thereof;

(c) extracting the accumulated oil from the oil-producing microbial biomass and the oil-producing algal biomass using organic solvent or thermopressurized direct liquefaction; and

(d) reacting the extracted oil with an alcohol to produce the biodiesel and/or fuel oil.

2. The process of claim 1, wherein

in step a), the oil-producing microbe is Rhodosporidium toruloides, and wherein the cultivating results in a residual broth and production of CO₂;

and

in step b), the liquid effluent comprises said residual broth, the oil-producing algae is Botryococcus braunii, and wherein the cultivating comprises cultivating the algae with the CO₂ and the liquid effluent; and

further comprising;

prior to step (b) separating the oil-producing microbial biomass from the liquid effluent comprising the residual broth; and

transesterifying the extracted oils.

3. The process of claim 2, wherein the carbon source further comprises glycerol.

4. The process of claim 2, further comprising the step of preparing an inoculate of the strain Rhodosporidium toruloides in solid yeast medium (YM medium), and incubating the inoculate in an oven at 30°

C. for five days and incubation for a period of about 72 hours, the YM medium composed per volume thereof of 10 g/l glucose, 5.0 g/l peptone, 3.0 g/l yeast extract, 3.0 g/l malt extract, and 20 g/l agar, and said YM medium having a pH of 5.0.

5. The process of claim 2, wherein the cultivating the oil-producing microbial biomass comprises cultivating in a bioreactor provided with mechanical shaking for a period of 24 hours to 150 hours at a carbon:

nitrogen ratio between 0.5 and 500 (w/w), a pH between 2.5 and 8.5, a temperature between 10 and 50°

C., and aerating with a volume of air per volume of the biomass per minute (v/v/m) of 0.1 to 5 v/v/m.

6. The process of claim 2, wherein the cultivating the oil-producing microbial biomass comprises the steps of:

preparing a pre-inoculate medium comprising per volume thereof 10 g/l glucose, 5 g/l peptone, 3 g/l yeast extract, and 3 g/l malt extract;

preparing an adaptation medium comprising per volume thereof 10 g/l sugar cane molasses, 5 g/l concentrated and detoxified sugar cane bagasse hydrolysate (DHCB), 5 g/l glycerol, and 5 g/l yeast extract; and

preparing a propagation medium comprising per volume thereof 40 g/l sugar cane molasses, 30 g/l DHCB, 30 g/l glycerol, 5 g/l yeast extract, 2.5 g/l urea, and 0.5 ml/l antifoaming agent,

wherein all of the prepared media are prepared at a pH of about 5.0.

7. The process of claim 6, wherein the cultivating the algal biomass comprises the steps of:

adapting the algae in the residual broth in cultures incubating for a period of about fifteen days, during which period the algae is maintained at a temperature of 25±

2°

C., shaken at about 110 rpm, provided about 1500 Lux of lightning irradiation intensity for twelve-hour periods alternating with twelve hours of darkness, and wherein the algal biomass is formed, filtered, washed with distilled water, and then dried in an oven at about 100°

C. for 24 hours;

preparing an inoculate having about 0.2 g of the adapted algae per liter of the inoculate; and

activating the inoculate, in a photobioreactors containing the residual broth of the oil-producing microbial biomass, which are provided with;

shaking, aerating with a volume of atmospheric air per volume of the biomass per minute (v/v/m) of about 1 v/v/m, maintaining at a temperature between 30±

2°

C., illuminating with 1500 Lux, and cultivating for a period of time of fifteen days;

injecting the CO₂ from step (a) within photo bioreactors, which by bubbling the CO₂ so as to reach a concentration in dissolved form in the medium of about 0.1 to 30% (v/v); and

separating or harvesting the algal biomass produced, by centrifugation and/or filtering.

8. The process of claim 2, wherein the extracting of the accumulated oil comprises passing the oil-producing microbial biomass and the oil-producing algal biomass through a process of cellular disruption wherein the extracting optionally comprises extracting the accumulated oils through a Soxhlet extractor and/or by a direct thermopressurized liquefaction.

9. The process of claim 2 or 8, wherein the biodiesel is a transesterified biodiesel and wherein the transesterifying produces a residual glycerol which residual glycerol is recirculated to feed into a production bioreactor containing the oil-producing microbial biomass.

10. The process of claim 2 or 8, wherein the biodiesel and/or biooil are produced for direct use as fuels to generate heat and/or steam or as adjuvants to gross petroleum or heavy fractions thereof originating from refinement.

11. The process of claim 1, wherein in the step of cultivating the oil-producing microbial biomass comprises at least one filamentous fungi and/or yeast selected from the group consisting of Candida curvata, Candida guilhermondi, Candida tropicalis, Candida sp., Candida oleophila, Candida lipolitica, Cryptococcus terricolus, Hansenula saturnus, Hansenula ciferrii, Lipomyces starkeyi, Rhodosporidium toruloides (Rhodotorula gracilis), Aspergillus fischeri, Aspergillus fumigatus, Aspergillus nidulans, Aspergillus ochrceus, Aspergillus terreus, Aspergillus ustus, Cladosporium fulvum, Cladosporium herbarum, Mucor miehei, Penicillium gladioli, Penicillium javanicum, Penicillium lilacinum, Penicillium spinulosum, Penicillium ultimum, Cryptococcus albidus, Rhodotorula glutinis, Trichosporon pullulans, Mortierrella hygrophila, Mortierrella zychae, Mortierrella elongata, Mortierrella parvispora, Mortierrella schmuckeri, Mortierrella alpina, Lypomyces lipofer, Lipomyces tetrasporus, Williopsis saturnus, Candida diddensiae, Yarrowia lipolitica, and Trichosporon cutaneum.

12. The process of claim 1, wherein in the step of cultivating the oil-producing algal biomass comprises an algae and/or cyanobacteriae in an isolated culture or in co-cultures, and said algae and/or cyanobacteriae is selected from the group consisting of Euglena, Anabaena, Dunaliella, Achananthes, Amphora, Ankistrodesmus, Chaetoceros, Clorococcum, Chlorrella, Chromonas, Chrysosphaera, Cricophaera, Cryptomonas, Cyclotella, Navicula, Amphiprora, Eustigmatophyte, Pleuorochysis, Franceia, Gleocapsa, Gloeothamnion, Hymenomonas, Isochrysis galbana, Monoraphidium, Nannochloropsis, Nephrochloris, Nitzschia, Ochromonas, Oocystis, Oscillatoria, Phaeodactylum, Platymonas, Pleurochrysis, Prymnesiophyte, Pseudoanabaena, Pyraminonas, Stichococcus, Synechococcus, Tetraselmis, Thalassiosira, and mutant strains having all the identifying characteristics thereof that are able to accumulate lipids in their biomass.

13. The process of claim 12, wherein the algae and/or cyanobacteriae is selected from the group consisting of Euglena gracilis, Anabaena variabilis, Anabaena cylindrica, Anabaena hassali, Anabaena planctonica, Dunaliella salina, Dunaliella bardawil, Dunaliella tertioleta, Achananthes orientalis, Amphora delicatissima, Amphora cafeiformis, Ankistrodesmus falcatus, Chaetoceros muelleri, Chaetoceros gracilis, Chaetoceros muelleri, Chaetoceros subsalsum, Chlorrella ellipsoidea, Chlorrella salina, Cyclotella meneghiniana, Cyclotella cryptica, Navicula saprophil, Navicula pseudotenelloides, Navicula biskanterae, Navicula acceptata, Navicula saprophila, Navicula pseudotenelloides, Amphiprora hyalina, Eustigmatophyte flagellate, Nannochloropsis salina, Nitzschia pusilla, Nitzschia monoensis, Nitzschia elliptica, Nitzschia alexandrina, Nitzschia quadrangula, Nitzschia inconspicua, Nitzschia microcephala, Nitzschia frustulum, Nitzschia hantzchianna, Nitzschia intermedia, Nitzschia frustulum, Nitzschia communis, Oocystis pusilla, Oscillatoria subborevis, Oscillatoria limnetica, Phaeodactylum tricornutum, Pleurochrysis dentate, Tetraselmis suecica, Thalassiosira weissflogii, and mutant strains having all the identifying characteristics thereof that are able to accumulate lipids in their biomass.

14. The process of claim 1, wherein the residues of sugar cane are selected from the group consisting of concentrated and detoxified hydrolyzed sugar cane bagasse (DHCB), juice, molasses, brown sugar, and white sugar.

15. The process of claim 14, wherein the residues of sugar cane is sugar cane bagasse that has been subjected to pre-treatment, comprising (i) treating the sugar cane bagasse with physical means, physical/chemical means, chemical means, biological means, and combinations thereof, wherein the pre-treatment changes the size and structure of lignocellulose fibers, micro and macroscopically and the chemical composition and submicroscopic structure of the sugar cane bagasse before the sugar cane bagasse is hydrolyzed, and then (ii) hydrolyzing the sugar cane bagasse by chemical or enzymatic means.

16. The process of claim 15, wherein the treating (i) of the sugar cane bagasse comprises treating dry sugar cane bagasse particles of 0.1-0.8 mm in diameter, wherein the hydrolyzing (ii) comprises hydrolyzing the sugar cane bagasse at about 125°

C. for a period of about twenty minutes, and providing for each 1 kg of dry sugar cane bagasse about 120 grams of concentrated sulfuric acid and in a solid-liquid ratio of 1;

10 (w/v) thereby obtaining a hydrolysate, and further comprising concentrating and detoxifying the hydrolysate thereby obtaining said DHCB.