Photobioreactor
09644176 ยท 2017-05-09
Assignee
Inventors
Cpc classification
C12M31/10
CHEMISTRY; METALLURGY
C12M43/04
CHEMISTRY; METALLURGY
International classification
Abstract
A photobioreactor has an optical waveguide formed at least in part from a highly scattering optically transmitting polymer. The optical waveguide has a light distributing part immersed in a container holding photoactive biological material and a light collecting part outside the container.
Claims
1. A photohioreactor that uses sunlight as a light source, comprising: a container holding a photoactive biological material; and an optical waveguide at least partially located within the container; wherein the optical waveguide is formed at least in part from highly scattering optically transmitting polymer, and wherein the optical waveguide is formed with a light collecting part contacting a light distributing part, the light collecting part having a surface configured to collect the sunlight, wherein the light distributing part is formed as a sheet, wherein the light collecting part and the light distributing part have a fixed size ratio, and wherein the light collection part has a first surface configured to collect sunlight and second surface directly directing the collected sunlight into a side of the sheet that the light collection part contact.
2. The photohioreactor of claim 1 wherein the light distributing part is formed entirely from the highly scattering optically transmitting particles.
3. The photohioreactor of claim 1 wherein the light distributing part is located wholly within the container.
4. The photohioreactor of claim 1 wherein the light collecting part is located wholly outside the container.
5. The photobioreactor of claim 1 wherein the light collecting part and the light distributing part have a size ratio selected to provide a light dilution factor of about 2 to 10 times.
6. The photobioreactor of claim 1 wherein the waveguide includes at least a portion that is a flexible part.
7. The photobioreactor of claim 1 wherein the waveguide is doped with wavelength shifting dopant.
8. The photobioreactor of claim 1 wherein the container is a cell having at least one wall that is gas permeable and liquid impermeable.
9. The photobioreactor of claim 1, wherein the light distributing part is a sheet and the light collection part injects the collected sunlight along a side of the sheet.
10. The photobioreactor of claim 1 further comprising supplemental light sources that direct light into the waveguide.
11. The photobioreactor of claim 10 wherein the supplemental light sources are light emitting diodes positioned to inject light into the light distributing part along a side that is different from a side along which the light collecting part contacts the light distributing part.
12. A photobioreactor that uses sunlight, comprising: a container holding a photoactive biological material, and an optical waveguide at least partially located within the container, wherein the optical waveguide is formed as a sheet that has a light collecting part and a light distributing part, wherein the light distributing part is formed in part of a highly scattering optically transmitting polymer, wherein the light collection part has a surface configured to collect sunlight and to direct the collected sunlight into a side of the sheet that the light collection part contacts, and wherein the optical wave guide has only one light collecting part and one light distributing part, wherein the light collecting part and the light distributing part have a size ratio selected to provide a light dilution factor of about 2 to 6 times.
13. The photobioreactor of claim 12, wherein all of the light collected by the light collecting part is directed into the one light distributing part.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) To assist in understanding the invention and to enable a person skilled in the art to put the invention into practical effect, preferred embodiments of the invention will be described by way of example only with reference to the accompanying drawings, in which:
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DETAILED DESCRIPTION OF THE INVENTION
(10) Embodiments of the present invention reside primarily in a photobioreactor. Accordingly, the elements have been illustrated in concise schematic form in the drawings, showing only those specific details that are necessary for understanding the embodiments of the present invention, but so as not to obscure the disclosure with excessive detail that will be readily apparent to those of ordinary skill in the art having the benefit of the present description.
(11) In this specification, adjectives such as first and second, left and right, and the like may be used solely to distinguish one element or action from another element or action without necessarily requiring or implying any actual such relationship or order. Words such as comprises or includes are intended to define a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed, including elements that are inherent to such a process, method, article, or apparatus.
(12) Referring to
(13) Sunlight collected by the light collecting part 111 is guided to the light distributing part 112. The light distributing part 112 is formed from highly scattering optical transmission (HSOT) polymer. HSOT polymers are formed by introducing heterogeneous structures on the order of microns into photonics polymers. These micro-structures are too small to be discernible but for the purpose of exemplification are shown as dots 113 in
(14) The light collecting part 111 of the waveguide is shaped to maximize light capture for a given location. The inventor envisages the light collecting part 111 being specifically designed for a particular location such that each location will have a different shaped light collecting part 111. The captured sunlight is directed into the light distributing part 112. It is anticipated that in most situations the intensity of light directed to the light distributing part 112 would be 4 to 5 times too intense for most species of micro-algae. However, the size ratio of the light collecting part 111 to the light distributing part 112 means that the collected sunlight is distributed over an area 4 to 5 times greater than the collection area, thus diluting the light to a level that is not detrimental to the micro-algae while at the same time distributing the light to a greater depth. The HSOT polymer achieves homogeneous distribution of light into the container 12.
(15) Depending on the specific design of the light collecting part 111 and the size of the light distributing part 112, the light dilution factor may be about 2 times, or 3 times, or 4 times, or 5 times, or 6 times. The invention is not limited to these specific values but the inventor envisages that in many applications these values will be typical.
(16) The light collecting part 111 may be produced from a flexible polymer so that it can be flexed to track the sun. Alternatively only a portion, such as the portion indicated as 114 in
(17) Alternatively the light collecting part 111 may be formed from a rigid light transmitting material such as glass or a rigid polymer. Rigid polymeric materials that may be used include, for example, thermoplastic polymers such as polycarbonates, poly(meth)acrylates such as polymethyl methacrylate, polyolefins such as polyethylene and polypropylene, polyesters such as polyethyleneterephthalates and polyethylenenaphthalates, celluloseacetate, polyvinyl chloride, and copolymers of acrylonitrile, styrene and butadiene.
(18) Whether the light collecting part 111 is rigid or flexible it may be useful to allow it to move relative to the light distributing part 112 in a manner which tracks the sun to optimise the amount of incident sunlight throughout the day. Whatever the actual connection between the light collecting 111 and light distributing 112 parts, it should not significantly diminish the transmittal of received light between these parts while allowing for the necessary sun tracking movement.
(19) Even with the use of solar tracking technology to maximise sunlight collection it may be the case that prolonged overcast periods or other low light conditions means that the photobioreactor 10 does not operate efficiently. In such circumstances it may be advantageous to supplement sunlight by using supplemental light sources. One suitable supplemental light source is shown in
(20) A wide range of micro-algae are suitable for use in the photobioreactor. For example, lipid or oil-producing algae include a wide variety of algae, such as the diatoms (bacillariophytes), green algae (chlorophytes), blue-green algae (cyanophytes), and golden-brown algae (chrysophytes). Exemplary bacillariophytes capable of oil production include the genera Amphipleura, Amphora, Chaetoceros, Cyclotella, Cymbella, Fragilaria, Hantzschia, Navicula, Nitzschia, Phaeodactylum, and Thalassiosira. Exemplary chlorophytes capable of oil production include the genera Ankistrodesmus, Botryococcus, Chlorella, Chlorococcum, Dunaliella, Monoraphidium, Oocystis, Scenedesmus, and Tetraselmis. Exemplary cyanophytes capable of oil production include the genera Oscillatoria and Synechococcus. An example of a chrysophyte capable of oil production is the genera Boekelovia. A combination of two or more strains of algae can be used in the photobioreactor embodiments described herein.
(21) Many micro-algae have peak production efficiency in a narrow wavelength range. To maximise efficiency of the photobioreactor a wavelength shifting dopant may be incorporated into the light collecting part 111 of the waveguide 11. The dopant is chosen for the wavelength shift required for a given organism. Generally this will require a shift from the blue end of the spectrum (short wavelengths) to the red end of the spectrum (long wavelengths).
(22) The container 12 may contain water having simple organic carbon compounds that the given species of micro-algae are able to utilize. This may include acetic acid or simple sugars. This allows the bioreactor to be operated in a mixotrophic mode. That is, part of the bioreactor operates in autotrophic (photosynthetic) mode and part in heterotrophic (respirating) mode. It has been reported that mixotrophic mode can produce 3 to 4 times the biomass of autotrophic mode alone.
(23) The photobioreactor 10 may form part of a closed system with the fluid medium supporting micro-photosynthetic organisms on each side of the light distributing part 112 constrained by gas permeable membranes. The membranes define a photobioreactor container that contains the growth media. The photobioreactor 10 is then placed within a gas carrying duct. The carbon dioxide rich flue gas is directed over the gas permeable membranes of the photobioreactor 40. Gas exchange with the media within the membrane occurs based on concentration gradients. The media acts as a sink of carbon dioxide, some oxides of nitrogen, and oxides of sulphur. The appropriate photosynthetic organism is selected for the particular gas mix being treated.
(24) As mentioned above, the photobioreactor 10 may be an open system or a closed system, such as a number of photobioreactors 40 as shown in
(25) In
(26) In an open system the container 12 will generally be larger, such as a pond. To maximise production a larger surface area of waveguide 11 is required. The waveguides may be stacked such as shown in
(27) In the embodiment shown in
(28) A further embodiment of the waveguide is shown in
(29) A yet further embodiment of a waveguide is shown in
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(31) Certain embodiments may also use optical coatings on the waveguide to reduce or increase reflection as required. For instance, in the embodiment of
(32) A technical advantage of the invention described here is that it allows the dilution of sunlight in a manner that prevents the waste of available light. Dilution of the light also eliminates the need to provide energy intensive mixing to prevent light fatigue of the photo-organisms. Distribution of sunlight deeper into a photobioreactor allows algal growth at greater depth than hitherto achievable.
(33) The invention will find many applications. One example is to economically treat municipal and industrial wastewaters using mixotrophic micro-algae to produce renewable fuel feedstock. Such an application can be incorporated in new designs for wastewater treatment facilities or retrofitted to existing facilities. This approach provides water utilities with a method of reducing their greenhouse gas footprint and to recover dilute resources from wastewaters.
(34) The above description of various embodiments of the present invention is provided for purposes of description to one of ordinary skill in the related art. It is not intended to be exhaustive or to limit the invention to a single disclosed embodiment. As mentioned above, numerous alternatives and variations to the present invention will be apparent to those skilled in the art of the above teaching. Accordingly, while some alternative embodiments have been discussed specifically, other embodiments will be apparent or relatively easily developed by those of ordinary skill in the art. Accordingly, this invention is intended to embrace all alternatives, modifications and variations of the present invention that have been discussed herein, and other embodiments that fall within the spirit and scope of the above described invention.