Source: https://patents.google.com/patent/US20100261918A1/en
Timestamp: 2019-02-19 11:22:03
Document Index: 787957139

Matched Legal Cases: ['Application No. 20080160593', 'Application No. 20090043118', 'Application No. 20090000941', 'Application No. 20080160593', 'Application No. 20090043118', 'Application No. 20090000941']

US20100261918A1 - Novel Process for Separating Lipids From a Biomass - Google Patents
Novel Process for Separating Lipids From a Biomass Download PDF
US20100261918A1
US20100261918A1 US12/758,480 US75848010A US2010261918A1 US 20100261918 A1 US20100261918 A1 US 20100261918A1 US 75848010 A US75848010 A US 75848010A US 2010261918 A1 US2010261918 A1 US 2010261918A1
US12/758,480
US8476060B2 (en
2009-04-13 Priority to US16880409P priority Critical
2010-04-12 Application filed by University of Texas System filed Critical University of Texas System
2010-04-12 Priority to US12/758,480 priority patent/US8476060B2/en
2010-06-15 Assigned to BOARD OF REGENTS, THE UNIVERSITY OF TEXAS SYSTEM reassignment BOARD OF REGENTS, THE UNIVERSITY OF TEXAS SYSTEM ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: CHIANELLI, RUSSELL R., HILDEBRAND, CALVIN, RODRIGUEZ, JOAQUIN
2010-10-14 Publication of US20100261918A1 publication Critical patent/US20100261918A1/en
2013-07-02 Publication of US8476060B2 publication Critical patent/US8476060B2/en
A novel low cost separation process for separating lipid oil from an algal biomass for biofuel production is described herein. The process of the present invention comprises of two steps: (i) breaking the algae cells and (ii) separation of the lipid oils from the broken cells. The separated lipids are extracted by conventional techniques followed by conversion to a biofuel.
This application claims priority to U.S. Provisional Application Ser. No. 61/168,804, filed Apr. 13, 2009, the entire contents of which are incorporated herein by reference.
The present invention relates in general to the field of biofuel production from a biomass, and more particularly, to a novel low cost separation process for separating lipid oil from an algal biomass.
Without limiting the scope of the invention, its background is described in connection with a novel separation process for separating lipid oils from an algal biomass.
Approximately, two-thirds of the petroleum imported into the U.S. comes from the Middle East primarily from Saudi Arabia and Iran. This dependence on Middle Eastern oil shackles U.S foreign policy. Elimination of the U.S. dependence will involve hard work and multiple approaches. One popular approach towards energy independence is the transformation to alternate energy sources such as biodiesel1 produced from various biomasses.
There are many biomasses that could potentially be used to produce biodiesel. However, biodiesel production from microalgal lipids has proven to be very promising. Production of oil from microalgae has been described in US Patent Application No. 20080160593 (Oyler, 2008).2 The application describes a process for production of biofuels from algae that includes cultivating an oil-producing algae by promoting sequential photoautotrophic and heterotrophic growth. The method can further include producing oil by heterotrophic growth of algae wherein the heterotrophic algae growth is achieved by introducing a sugar feed to the oil-producing algae. The algal oil can be extracted from the oil-producing algae, and can be converted to form biofuel.
US Patent Application No. 20090043118 (Kozyuk, 2009)3 describes a method comprising applying a controlled flow cavitation apparatus to a biodiesel production process in order to increase fatty acid alkyl ester yield. A feedstock comprising free fatty acids can be passed through a controlled flow cavitation apparatus at a velocity capable of generating a hydrodynamic cavitation zone where the free fatty acids can be esterified. One or more controlled flow cavitation apparatuses can be applied at various points of a biodiesel production process.
US Patent Application No. 20090000941 (Kropf, 2009)4 describes an invention relating generally to chemical reactions and processes, and in particular to a method for enhancing the rate of a chemical reaction and to apparatus for carrying out the method. The invention more particularly relates to methods and apparatus which utilize microwave and ultrasonic energy to enhance chemical reaction rates; and in specific instances, the invention relates to methods, processes and apparatus for the synthesis of biodiesel fuels. The methods, processes and apparatus of the invention are useful for the synthesis of biodiesel fuels; and also useful for production of reaction products of esterification and/or transesterification reactions including fatty acid alkyl esters.
The separation of lipid oil from algae is a major issue in developing biofuels from algae. The present invention describes a two stage process to (i) breaking of the algae cells and (ii) separation of the lipid oils from the broken cells. In the first step, a sonic device known as a SOLOTON is used to break the algae cells creating a completely dispersed emulsion “pea soup” of broken algae cells, lipids, and growth media. In the second step, a novel chemical treatment with acid released the lipid oil from the “pea soup” and at least two phases (lipid oil/water dispersed broken cells) are created. The oil may then be extracted with conventional techniques.
In one embodiment, the present invention describes a process for lysing one or more microalgal cells, wherein the lysis results in the extraction of one or more algal lipids. The process comprises the steps of: (i) cultivating a hydrocarbon or a lipid-producing microalgae in a growth media, wherein the cultivation is carried out under one or more growth conditions comprising sunlight, nutrients, water, and CO2, (ii) exposing the microalgae to low energy soundwaves in a sonicating device (e.g., using a sonic device) to produce a homogenous algal slurry comprising broken algal cells, algal lipids and the growth media, wherein the homogeneous algal slurry comprises a lipid/oil top layer, a green layer comprising lysed microalgal cells and a clear water layer, (iii) extracting one or more algal lipids from the algal slurry by a chemical treatment, wherein the chemical treatment may include, but is not limited to the addition of heat, acid, and chemicals to break an oil/water emulsion, (iv) exposing the homogeneous algal slurry to low energy soundwaves in the sonicating device to break the oil/water emulsion, wherein the exposure of the homogeneous algal slurry to low energy soundwaves is an optional treatment step, and (v) extracting of the one or more algal lipids.
In one aspect the process further comprises the step of converting the extracted one or more algal lipids to a renewable fuel or a biofuel. In another aspect of the present invention the sonicating device is a SOLOTON device. In further aspects the low energy soundwaves have a maximum frequency of 2 MHz and the flow rate of the microalgal cells suspended in the growth media into the SOLOTON is varied. In yet another aspect the acids used to extract the one or more algal lipids from the algal slurry are selected from at least one of nitric acid, sulfuric acid, hydrochloric acid, phosphoric acid, acetic acid, inorganic acids or organic acids used in concentrations of 0.01M, 0.05M, 0.1M, 0.25M, 0.5M, 0.75M, and 1.0M
In a further aspect the lipid-producing algae includes an algae selected from the group consisting of diatoms (bacillariophytes), green algae (chlorophytes), blue-green algae (cyanophytes), golden-brown algae (chrysophytes), haptophytes, and combinations thereof. In a specific aspect the lipid-producing algae is selected from one or more of Amphipleura, Amphora, Chaetoceros, Chlorella, Cyclotella, Cymbella, Fragilaria, Hantzschia, Navicula, Nitzschia, Phaeodactylum, Thalassiosira, Ankistrodesmus, Botryococcus, Chlorella, Chlorococcum, Dunaliella, Monoraphidium, Oocystis, Scenedesmus, Tetraselmis, Oscillatoria, Synechococcus, Boekelovia, or combinations thereof.
In one aspect the present invention describes a step of converting algal oil into the renewable fuel or the biofuel by direct hydrogenation of the algal oil to produce the biofuel. In a related aspect the step of converting algal oil into biofuel comprises the conversion of lipid to biofuel by transesterfication of the algal oil to produce the biofuel.
One aspect of the present invention is directed towards forming a lipid product formed by the process described in the embodiment of the present invention. In related aspects the lipid product is substantially free of sulfur, comprises a fatty acid ethyl ester, and an alkane.
In another embodiment the present invention describes a system for production of a renewable fuel or a biofuel from one or more microalgae, comprising: one or more microalgal growth reservoirs, one or more microalgal homogenizers connected to the reservoirs, the homogenizers comprising an apparatus that creates a homogenous slurry comprising broken microalgal cells, growth media, and algal lipids by breaking the microalgal cells using low energy soundwaves to produce the homogeneous algal slurry, one or more algal lipid extraction vessels connected to the homogenizers, wherein the algal lipids are extracted by a chemical treatment; wherein the chemical treatment may include, but is not limited to the addition of heat, acid, and chemicals to break an oil/water emulsion and one or more converters connected to the extracted algal lipid vessel, wherein the algal lipids are converted into the renewable fuel or the biofuel.
In a related aspect the one or more converters are configured for conversion by direct hydrogenation of the algal oil to produce the renewable fuel or the biofuel. In another aspect the one or more converters are configured for conversion by transesterfication of the algal oil to produce the renewable fuel or the biofuel. In yet another aspect the algae are grown under conditions that stimulate accumulation of lipids selected from at least one of light stimulation, nutrient stimulation, injection of a reactive carbon dioxide source, and nutrients. The microalgae used in the system of the instant invention include an algae selected from the group consisting of diatoms (bacillariophytes), green algae (chlorophytes), blue-green algae (cyanophytes), golden-brown algae (chrysophytes), haptophytes, and combinations thereof.
FIG. 1 is a schematic showing the process of biofuel production in algae;
FIG. 2 is a schematic of the present invention showing the use of the SOLOTON sonic device for biofuel production in algae;
FIG. 3 shows the use of the SOLOTON sonic device as envisioned by the present invention;
FIG. 4 represents the algal biomass before and after the treatment in the SOLOTON sonic device: (A) before treatment in the SOLOTON the algal biomass solution has two phases (water on top and algae at the bottom), and (B) after the SOLOTON the solution is homogenous and has the consistency of “pea soup”; and
FIGS. 5A and 5B shows the effect of a simple chemical treatment on the treated and untreated samples shown in FIG. 4: (FIG. 5A) in the sample treated by the SOLOTON the “pea soup” separated in to three layers; (i) lipid/oil on the top, (ii) a very thin green layer, and (iii) the water layer and (FIG. 5B) in the untreated layer no separation is observed. The thin green layer between the lipid/oil layer and the water layer consists of disrupted algal cell walls.
As used herein the term “algae” represents a large, heterogeneous group of primitive photosynthetic organisms which occur throughout all types of aquatic habitats and moist terrestial environments. Nadakavukaren et al., Botany. An Introduction to Plant Biology, 324-325, (1985). The term “algae” as described herein is intended to include the species selected from the group consisting of the diatoms (bacillariophytes), green algae (chlorophytes), blue-green algae (cyanophytes), golden-brown algae (chrysophytes), haptophytes, freshwater algae, saltwater algae, Amphipleura, Amphora, Chaetoceros, Cyclotella, Cymbella, Fragilaria, Hantzschia, Navicula, Nitzschia, Phaeodactylum, Thalassiosira Ankistrodesmus, Botryococcus, Chlorella, Chlorococcum, Dunaliella, Monoraphidium, Oocystis, Scenedesmus, Nanochloropsis, Tetraselmis, Chlorella, Dunaliella, Oscillatoria, Synechococcus, Boekelovia, Isochysis and Pleurochysis. The term “homogenizer” is used in the general sense of a grinder, and often no pressure limitations or initial, i.e. prehomogenization, particle size required in order to achieve the desired particle size are specified.
The term “microalgae” as used herein includes all forms of microscopic aquatic plants including mixtures of Green and Bluegreen Algae, preferably uni-cellular non-filamentous noncolonial types, to which photosynthetic bacteria may also be added. The term “microalgae” also refers to algae that are smaller than approximately 2 centimeters in height or length.
The term “interface” as used herein indicates a boundary between any two immiscible phases. The term “lysing” refers to the action of rupturing the cell wall and/or cell membrane of a cell. The term “lysing” does not require that the cells be completely ruptured, rather, “lysing” can also refer to the release of intracellular material.
As used herein the term “esterification” or “transesterification” are the processes by which an acid group is added, hydrolyzed, repositioned or replaced on one or more components of the substrate. The acid group can be derived from a fat or oil which is part of the initial substrate, or from a free fatty acid or ester that has been added to the deodorized substrate or purification media-processed substrate. The term “transesterification ” includes the process in which R, R′ or R″ on a glyceride is a first fatty acid group given by —OC(═O)R′″, and the first fatty acid group is replaced by a second, different fatty acid group. The second fatty acid group which replaces the first fatty acid group can come from the same or different fat or oil present in the initial substrate. The second fatty acid can also come from a free fatty acid or ester added to the deodorized substrate or the purification media-processed substrate.
The term “biodiesel” used in this specification includes mono alkyl esters of a long chain fatty acid derived from renewable lipid sources. Suitable sources include animal fats and vegetable oils, including, for example, soybean oil, sunflower oil, linseed oil, coconut oil, and the like. Other useful biodiesel materials for use in the present invention comprise a mixture of fatty acid esters. Typically these materials are made by the transesterification of vegetable oil to biodiesel. One route to biodiesel involves reacting a vegetable oil (a triglyceride) with an alcohol, preferably methanol, to form biodiesel and glycerol. Biodiesels can comprise methyl esters that contain, for example, C6-C14 fatty acids such as caproic, caprylic, capric, lauric, and myristic. The term “biodiesel ” can also include, for example, methyl esters of C12-C22 fatty acids such as lauric acid, myristic acid, palmitic acid, palmitoleic acid, stearid acid, oleic acid, elaidic acid, petroselic acid, ricinoleic acid, elaeosteric acid, linoleic acid, linolenic acid, arachic acid, gadoleic acid, behenic acid and erucic acid. It should be understood however, that, in other embodiments, other useful biodiesel materials and mixtures of these and other biodiesels, are within the contemplated scope of the present invention.
As used herein, the term “biofuel” or “biomass” refers to organic matter harvested or collected as a source of energy. Specifically, biofuel refers to a source material that is derived from non-fossilized organic matter and available on a renewable or recurring basis, as compared with a fossil fuel, which is derived from fossilized organic matter and is not considered to be “renewable.” Biofuels are typically obtained from production waste streams, i.e., production byproducts, although they can also be obtained from sources specifically designed to produce biofuels. There are generally considered to be three types of biofuels, namely, agricultural biofuels (defined below), municipal waste biofuels (residential and light commercial garbage or refuse, with most of the recyclable materials such as glass and metal removed) and forestry biofuels (e.g., trees, waste or byproduct streams from wood products, wood fiber, pulp and paper industries). Biofuels also encompass either a 100% biodiesel or a mixture comprising biodiesel and regular petroleum-based diesel from a refinery
The instant invention describes a two stage process herein below for breaking or lysing one or more algae cells and for the separation of the lipid oils from the broken cells. In a first step, a sonic device known as a SOLOTON is used to break the algae cells creating a completely dispersed emulsion “pea soup” of broken algae cells, lipids, and growth media. This is followed by a novel chemical treatment step wherein the acid released the lipid oil from the “pea soup” and at least two phases (lipid oil/water dispersed broken cells) are created. The oil can then be extracted with conventional techniques.
The need for new liquid fuel sources is evident everyday in the news and at the gas pump. Entire industries including airlines and trucking are at risk because of rapidly rising fuel prices and undependable oil exporters in the Middle East and Africa. In February of 2006, President Bush stated that the United States of America must break its dependence on petroleum (“America is addicted to oil”).1 Approximately two-thirds of the petroleum imported into the U.S. comes from the Middle East primarily from Saudi Arabia and Iran. This dependence on Middle Eastern oil shackles U.S foreign policy. Elimination of the U.S. dependence will involve hard work and multiple approaches. Solving this problem requires new technologies to produce substitutes for gasoline, diesel, and jet fuel. The Chairman of the Advisory Board of the Clean Fuels Foundation believes that this transformation should be coupled with a transformation to alternate energy sources such as biodiesel.5
The current political climate in the U.S. is urging a shift to independence from foreign oil sources and an overall understanding for the need to seek out new energy sources is becoming more prevalent among the general public. The shift to alternative fuels is exemplified by The Energy Development for a Growing Economy (EDGE) bill introduced in the senate in May 2006 which calls for 25% of vehicles sold in the U.S. to run on an alternative fuel by the year 2010.6 Because, biodiesel can be used with little or no modifications required on diesel engines, minor manufacturing technology and infrastructure modifications to the petroleum economy are needed for biofuels to gain significant market share.7 The transformation to alternate energy sources such as biodiesel will result in a significant decrease in CO2 greenhouse gas emission. Thus, the introduction of biodiesel will help accomplish the dual goal of energy security and improvement of the environment.
Over the next 20 years, energy consumption in the U.S. is projected to rise by 30%; yet domestic energy production is only expected to grow by 25%. Petroleum imports already supply more than 55% of U.S. domestic needs, and they are expected to grow to more than 68% by 2025 as worldwide oil demand continues to rise and domestic oil production continues to decline. This increased reliance on imported sources of energy threatens national security, the economy and future competitiveness. The alternative energy industry is therefore poised for growth. Biodiesel offers many advantages over traditional petroleum diesel in that it is made from renewable resources (biomass), is biodegradable, nontoxic and contains no sulfur. Although relatively new, growth in the U.S. biodiesel industry has gone from 2 million gallons in 2000, 25 million gallons in 2004, 91 million gallons in 20055 and these increases are expected to accelerate.
Because, biodiesel can be used with little or no modifications required on diesel engines, only minor manufacturing technology and infrastructure modifications are needed for this particular biofuel to gain significant market share.5 Biodiesel offers many advantages over traditional petroleum diesel in that it is made from renewable resources (biomass), is biodegradable, is nontoxic, and contains no sulfur. Although relatively new, US biodiesel production has gone from 2 million gallons in 2000, 25 million gallons in 2004, to 91 million gallons in 20058 and is growing at an exponential rate.
A variety of biomass sources are presently being used to produce biodiesel including soybeans, rapeseed, jatropha, and palm oil. There are many biomasses that could potentially be used to produce biodiesel. However, biodiesel production from micro-algal lipids has proven to be very promising. In 1998, the National Renewable Energy Laboratory completed a review of the Aquatic Species Program (ASP 1976-1996) to develop renewable transportation fuels from algae.9 The program catalogued progress in the biology; biochemistry and engineering of lipid producing algae grown in open ponds. However, at the writing of the report the price of oil was fluctuating between $20 and $25 per barrel of oil.10 Thus, the economic viability of biodiesel from algae was marginal in 1998. This situation is significantly different at the current $100-150 per barrel.
Present efforts to commercialize microalgae for biodiesel production are based on 20 years of federally funded work under the Aquatic Species Program (ASP 1976-1996). The data in Table 1 compares the number of US gallons that may be produced annually per acre by different “bio-fuel” crops. Microalgae can produce from 7 to 400 times more fuel per acre than any terrestrial plant because they are more efficient lipid producers and grow more rapidly. Many of the species of microalgae collected during the Aquatic Species Program (ASP) produced up to 60% of their body weight in the form of lipids that could then be converted into biodiesel.
Estimated Liquid Fuel Production Per Acre Per Year for Various
Biomass Crops.11-13
ENERGY CROP (US Gals/acre/year)
Soybean 40-50
Rapeseed 110-145
Jatropha 175
Switchgrass 1500
Palm Oil 650
Algae 10,000-20,000
Sugar Beet 714
The scalable impact of commercial biodiesel production from microalgae is exemplified by the fact that cultivation of microalgae over a surface of 38,500 km2 in a zone of high sun-exposure such as the Sonora Desert would make it possible to replace all US petroleum consumption.
A report investigating available underutilized saline water supplies, large areas of underutilized land and climatic conditions identified the US Southwest as ideally suited for the farming of microalgae for biofuel production from algal lipids.14 Furthermore, the use of brackish water and low-valued land would not compete with agriculture or cities for freshwater and desirable land.
The work performed under the Aquatic Species Program identified algae species best suited for biodiesel production; little research was conducted on downstream processes such as the large-scale (economical) harvesting of algae, extraction of lipids from algae, and commercial-scale production of high value products like lubricants, healthcare products, and biodiesel from microalgal oils and lipids. Separation of the algae and extraction of the lipid from the algae represent 30% or more of the cost of producing biofuel.5
FIG. 1 is a schematic representation 100 detailing the production of a biofuel from an algal biomass. In the first step the biofuel producing algae are cultivated in a growth reservoir 102 under favorable growth conditions (water, sunlight, CO2, and nutrients), supplied through inlets 104, 106, and 108 to the reservoir 102. The algal biomass is harvested after a specified number of days and transferred to vessel 110. The algal biomass is separated and dried 112. This is followed by extraction of the product (oils and lipids) by traditional solid-liquid extraction techniques in an extraction vessel 114. The extracted product is further subjected to chemical processes for conversion to a biofuel 116. The biomass left over after the extraction of the oils and lipids is used as animal feed 118.
The present invention discloses a novel process for separation of lipids from algal biomass that has low energy input, is rapid, and uses low cost chemical reagents using a patented device known as a SOLOTON. The detailed description of which is found in U.S. Pat. No. 5,538,628 (Logan, 1996), relevant portions incorporated herein by reference.16 The unit pictured will process 2,000 BBL/day of liquid. The unit runs on standard 120 volt electric service and is driven by a normal stereo amplifier with a specialized waveform input to produce sound waves. Because the SOLOTON operates on 120 volts, the energy input is very low in contrast with other sono-chemical processes in which the energy input is prohibitive. The algal slurry passes through the SOLOTON rapidly and produces homogenous algal slurry now composed of broken algal cells and released algal lipids. The SOLOTON affects this emulsification process as opposed to breaking chemical bonds.
FIG. 2 is a schematic representation of the method 200 of the present invention, showing the use of the SOLOTON device 210 in the production of a biofuel from an algal biomass. The biofuel producing algae are cultivated in a growth reservoir 202 in the presence of sunlight. Additional nutrients, water, and CO2, are supplied to the reservoir 202 through the inlets 204, 206, and 208. After allowing a specified amount of time for growth in the reservoir 202, the algal biomass is passed through the SOLOTON device 210 for processing. The processed sample forms a “pea soup” 214 comprising of three layers: lipid/oil on top, a very thin green layer, and then the water layer. The lipid/oil top layer is separated using traditional separation techniques (acid extraction, etc) and the extracted oil is subjected to further processing to produce the biofuel 216. The biomass left over after the extraction of the oils and lipids is used as animal feed 218
FIG. 3 is a schematic representation 300 of the end products after SOLOTON device processing 306 and emulsion separation chemistry 308. The sample 304 after the SOLTON 306 has three distinct layers a lipid/oil layer 312, a layer containing the algal biomass 314, and a water layer 310. The SOLOTON process 306 as detailed by the present invention obviates the step of drying and conventional separation of the algal biomass 314 from the product.
FIG. 4 represents the algal biomass before 402 and after 412 the treatment in the SOLOTON sonic device: (a) before treatment in the SOLOTON the algal biomass solution has two phases (water on top 404 and algae 406 at the bottom), and (b) after the SOLOTON the solution is homogenous and has the consistency of “pea soup” 414.
FIGS. 5A and 5B shows the effect of a simple chemical treatment 528 and 630 on the treated 512 and untreated 602 samples shown in FIG. 4, respectively. In the sample 512 treated by the SOLOTON, the “pea soup” 514 separated into three layers: lipid/oil on top 516, a very thin green layer 518, and then the water layer 520. The thin green layer 518 between the lipid/oil layer 516 and the water layer 520 consists of disrupted algal cell walls. In the untreated samples 602 no separation is observed.
Due to the simplicity, rapidness and low cost of this process, the present invention represents a significant advance over existing techniques for separating and recovering algal lipids.
1 MSNBC News Services Feb. 1, 2006
2 US Patent Application No. 20080160593.
3 US Patent Application No. 20090043118.
4 US Patent Application No. 20090000941.
5 R. James Woolsey personal communication July 2006.
6 D. Looker, Congress unleashes flurry of domestic ethanol support, http://www.agriculture.com/ag/story.jhtml?storyid=/templatedata/ag/story/data/1147894145821. xml, May 17, 2006
7 A. Karsner, Hydrogen Economy, http://www.eere.energy.gov/news/speeches/2006-05-16_hydrogen.cfm, May 16, 2006.
8 T. Dorr, Biofuels for Transportation Conference, http://www.worldwatch.org/node/4094?page=0%2C7, Jun. 13, 2006.
9 J. Sheehan, T. Dunahay, J. R. Benemann, and P. Roessler, A Look Back at the U.S. Department of Energy's Aquatic Species Program-Biodiesel from Algae” National Renewable Energy Laboratory, 1998.
10 OPEC and the High Price of Oil, Joint Economic Committee United States Congress, Chairman Jim Saxton, 2005.
11 http://www.unh.edu/p2/biodiesel/article—algae.html.
12 http://www.globalfootprints.org/isues/local/transport/biofuels.htm.
13 http://bioenergy.ornl.gov/papers/misc/switgrs.html.
14 E. L. Maxwell, A. G. Folger, S. E. Hogg. 1985. Resource evaluation and site selection for microalgae production systems. Solar Energy Research Institute, Golden.
15 M. E. Grima, E. H. Belarbi, F. G. Acien Fernandez, and A. Robles Medina. Recovery of microalgal biomass and metabolites: process options and economics. Biotechnology Advances. 20 (2003): 491-515.
16 U.S. Pat. No. 5,538,628.
1. A process for lysing one or more microalgal cells, wherein the lysis results in an extraction of one or more algal lipids, comprising the steps of:
cultivating a hydrocarbon or a lipid-producing microalgae in a growth media, wherein the cultivation is carried out under one or more growth conditions comprising sunlight, nutrients, water, and CO2;
exposing the microalgae to low energy soundwaves in a sonicating device to produce a homogenous algal slurry comprising broken algal cells, algal lipids, and the growth media, wherein the homogeneous algal slurry comprises a lipid/oil top layer, a green layer comprising lysed microalgal cells, and a clear water layer;
extracting one or more algal lipids from the algal slurry by a chemical treatment, wherein the chemical treatment may include, but is not limited to the addition of heat, acid, and chemicals to break an oil/water emulsion;
exposing the homogeneous algal slurry to low energy soundwaves in the sonicating device to break the oil/water emulsion, wherein the exposure of the homogeneous algal slurry to low energy soundwaves is an optional treatment step; and
extracting of the one or more algal lipids.
2. The process of claim 1, further comprising the step of converting the extracted one or more algal lipids to a renewable fuel or a biofuel.
3. The process of claim 2, wherein the step of converting algal oil into the renewable fuel or the biofuel comprises the conversion of lipid to the biofuel by direct hydrogenation of the algal oil to produce the biofuel.
4. The process of claim 2, wherein the step of converting algal oil into biofuel comprises the conversion of lipid to biofuel by transesterfication of the algal oil to produce the biofuel.
5. The process of claim 1, wherein the sonicating device is a SOLOTON device.
6. The process of claim 1, wherein the low energy soundwaves have a maximum frequency of 2 MHz.
7. The process of claim 1, wherein the flow rate of the microalgal cells suspended in the growth media into the SOLOTON is varied.
8. The process of claim 1, wherein the acids used to extract the one or more algal lipids from the algal slurry are selected from at least one of nitric acid, sulfuric acid, hydrochloric acid, phosphoric acid, acetic acid, inorganic acids or organic acids.
9. The process of claim 1, wherein the acids used to extract the one or more algal lipids are used in concentrations of 0.01M, 0.05M, 0.1M, 0.25M, 0.5M, 0.75M, and 1.0M
10. The process of claim 1, wherein the lipid-producing algae includes an algae selected from the group consisting of diatoms (bacillariophytes), green algae (chlorophytes), blue-green algae (cyanophytes), golden-brown algae (chrysophytes), haptophytes, and combinations thereof.
11. The process of claim 1, wherein the lipid-producing algae is selected from one or more of Amphipleura, Amphora, Chaetoceros, Chlorella, Cyclotella, Cymbella, Fragilaria, Hantzschia, Navicula, Nitzschia, Phaeodactylum, Thalassiosira, Ankistrodesmus, Botryococcus, Chlorella, Chlorococcum, Dunaliella, Monoraphidium, Oocystis, Scenedesmus, Tetraselmis, Oscillatoria, Synechococcus, Boekelovia, or combinations thereof.
12. A lipid product formed by the process of claim 1.
13. The lipid of claim 12, wherein the lipid product is substantially free of sulfur.
14. The lipid of claim 12, wherein the lipid product comprises a fatty acid ethyl ester.
15. The lipid of claim 12, wherein the lipid product comprises an alkane.
16. A system for production of a renewable fuel or a biofuel from one or more microalgae, comprising:
one or more microalgal growth reservoirs;
one or more microalgal homogenizers connected to the reservoirs, wherein the homogenizers comprise an apparatus that creates a homogenous slurry comprising broken microalgal cells, growth media and algal lipids by breaking the microalgal cells using low energy soundwaves to produce the homogeneous algal slurry;
one or more algal lipid extraction vessels connected to the homogenizers, wherein the algal lipids are extracted by a chemical treatment; wherein the chemical treatment may include, but is not limited to the addition of heat, acid, and chemicals to break an oil/water emulsion and
one or more converters connected to the extracted algal lipid vessel, wherein the algal lipids are converted into the renewable fuel or the biofuel.
17. The system of claim 16, wherein the one or more converters are configured for conversion by direct hydrogenation of the algal oil to produce the renewable fuel or the biofuel.
18. The system of claim 16, wherein the one or more converters are configured for conversion by transesterfication of the algal oil to produce the renewable fuel or the biofuel.
19. The system of claim 16, wherein the algae are grown under conditions that stimulate accumulation of lipids selected from at least one of light stimulation, nutrient stimulation, injection of a reactive carbon dioxide source, and nutrients.
20. The system of claim 16, wherein the microalgae include an algae selected from the group consisting of diatoms (bacillariophytes), green algae (chlorophytes), blue-green algae (cyanophytes), golden-brown algae (chrysophytes), haptophytes, and combinations thereof.
US12/758,480 2009-04-13 2010-04-12 Process for separating lipids from a biomass Active 2031-02-21 US8476060B2 (en)
US16880409P true 2009-04-13 2009-04-13
US12/758,480 US8476060B2 (en) 2009-04-13 2010-04-12 Process for separating lipids from a biomass
US13/907,539 US20130267722A1 (en) 2009-04-13 2013-05-31 Novel Process for Separating Lipids from a Biomass
US13/907,539 Division US20130267722A1 (en) 2009-04-13 2013-05-31 Novel Process for Separating Lipids from a Biomass
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US8476060B2 US8476060B2 (en) 2013-07-02
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US13/907,539 Abandoned US20130267722A1 (en) 2009-04-13 2013-05-31 Novel Process for Separating Lipids from a Biomass
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