US20200367458A1 - Algae cultivation systems and methods with reduced energy loss - Google Patents
Algae cultivation systems and methods with reduced energy loss Download PDFInfo
- Publication number
- US20200367458A1 US20200367458A1 US16/988,149 US202016988149A US2020367458A1 US 20200367458 A1 US20200367458 A1 US 20200367458A1 US 202016988149 A US202016988149 A US 202016988149A US 2020367458 A1 US2020367458 A1 US 2020367458A1
- Authority
- US
- United States
- Prior art keywords
- algae cultivation
- depth
- zone
- channel
- pump
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
Images
Classifications
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01G—HORTICULTURE; CULTIVATION OF VEGETABLES, FLOWERS, RICE, FRUIT, VINES, HOPS OR SEAWEED; FORESTRY; WATERING
- A01G33/00—Cultivation of seaweed or algae
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/02—Photobioreactors
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/02—Form or structure of the vessel
- C12M23/18—Open ponds; Greenhouse type or underground installations
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/38—Caps; Covers; Plugs; Pouring means
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M31/00—Means for providing, directing, scattering or concentrating light
- C12M31/08—Means for providing, directing, scattering or concentrating light by conducting or reflecting elements located inside the reactor or in its structure
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N1/00—Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
- C12N1/12—Unicellular algae; Culture media therefor
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01H—NEW PLANTS OR NON-TRANSGENIC PROCESSES FOR OBTAINING THEM; PLANT REPRODUCTION BY TISSUE CULTURE TECHNIQUES
- A01H13/00—Algae
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01H—NEW PLANTS OR NON-TRANSGENIC PROCESSES FOR OBTAINING THEM; PLANT REPRODUCTION BY TISSUE CULTURE TECHNIQUES
- A01H4/00—Plant reproduction by tissue culture techniques ; Tissue culture techniques therefor
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/80—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in fisheries management
Definitions
- the present disclosure relates generally to algae cultivation systems and methods, and more particularly to open raceway algae cultivation systems and methods.
- Algae cultivation has become widely recognized as a promising source of food, biofuel, chemicals, and nutraceuticals.
- Open algae cultivation systems have been developed for large-scale cultivation. The energy to operate a pump that circulates algae cultivation fluid or slurry is an important operating cost in these open systems. Larger open systems typically have a zone in a channel width entering the pump, and zone in a channel width exiting the pump. The bottom of the channels in these systems are typically level or gently sloped, so the speed of the algae slurry is much higher in the zones entering and exiting the pumps than the velocity in the rest of the channel. The acceleration and the high velocity both result in large energy losses. For level raceways, the energy losses are even greater than sloped systems.
- an open raceway algae cultivation system includes a channel configured to contain an algae cultivation fluid.
- the channel include a contraction zone having a width and a depth.
- a pump is configured to circulate the algae cultivation fluid in the channel and has an entrance and an exit.
- the width of the contraction zone decreases leading into the entrance of the pump, and the depth of the contraction zone is greater than a depth of at least a portion of the channel located outside of the contraction zone.
- an open raceway algae cultivation system in another aspect, includes a channel configured to contain an algae cultivation fluid.
- the channel including an expansion zone having a width and a depth.
- a pump is configured to circulate the algae cultivation fluid in the channel and includes an entrance and an exit. The width of the expansion zone increases going away from the exit of the pump and the depth of the expansion zone is greater than a depth of at least a portion of the channel located outside of the expansion zone.
- FIG. 1 is a plan view illustrating an open raceway algae cultivation system according to one embodiment of the present disclosure.
- FIG. 2 is a cross-sectional view taken along lines A-A of FIG. 1 .
- FIG. 3 is a plan view illustrating an open raceway algae cultivation system according to another embodiment of the present disclosure.
- FIG. 4 is a cross-sectional view taken along lines B-B of FIG. 3 .
- FIG. 1 illustrates one non-limiting embodiment of an open raceway algae cultivation system of the present disclosure.
- the system includes a channel 100 having two conduits 1 and 2 fluidly coupled or connected to each other by bends 3 a , 3 b .
- An algae cultivation fluid or slurry is contained with the channel and circulated by a pump 5 , which can be a paddlewheel, a propeller pump, an Archimedes screw pump, a fluid jet, or any other suitable structure or device for circulating or pumping the algae cultivation fluid through the channel 100 .
- a pump 5 can be a paddlewheel, a propeller pump, an Archimedes screw pump, a fluid jet, or any other suitable structure or device for circulating or pumping the algae cultivation fluid through the channel 100 .
- a width of pump 5 is less than a width of the conduits 1 and 2 so that leading into an entrance of the pump 5 there is a contraction zone 4 having a width that is less than a width of the channel 100 outside of the contraction zone 4 .
- the reduced width of contraction zone 4 decreases from the portion outside the contraction zone 4 leading into the entrance of the pump 5 .
- the width of pump 5 is also less than the conduits 1 and 2 so that going away from the exit of the pump 5 , there is an expansion zone 6 having a width greater than the width of channel 100 outside the expansion zone 6 .
- the increased width of expansion zone 6 increases going away from the exit of pump 5 .
- FIG. 2 is a cross-sectional view taken along lines A-A of the system of FIG. 1 illustrating a level bottom, variable depth contraction zone 4 , and a variable depth expansion zone 6 .
- the surface 7 of the algae cultivation fluid entering the pumping, and the surface 9 of the fluid exiting the pump 5 is open to the air.
- a bottom 8 of the channel 100 in the contraction zone 4 , and a bottom 10 of the channel 100 in the expansion zone 6 are sloped downwardly toward the pump 5 to maintain a substantially constant cross-sectional area.
- the pump 5 is illustrated as a paddlewheel, but the pump can be any device or structure suitable for increasing the algae cultivation fluid elevation from the surface 7 of the fluid entering the pump 5 to the surface 9 of the fluid exiting the pump 5 .
- the depth d 3 of fluid exiting the pump 5 is the greatest, while the depth of the fluid going away from the exit of the pump 5 decreases to d 4 so as to maintain a constant cross-sectional area of the algae cultivation fluid throughout the expansion zone 6 .
- the cross-sectional area of the algae cultivation fluid in the channel 100 can be defined as the depth of the algae fluid depth times a width of the channel 100 .
- the elevation of the surface 9 of the algae cultivation fluid decreases in the expansion zone 6 to overcome energy loss in the zone 6 .
- the algae cultivation fluid depth decreases from depth d 4 to depth d 1 to overcome energy loss in the channels 1 and 2 and bends 3 a and 3 b .
- the algae cultivation fluid depth increases to d 2 in the contraction zone 4 as the fluid leads into the entry of the pump 5 so as to maintain a substantially constant cross-sectional area in the contraction zone 4 .
- the elevation of the surface 7 of the algae cultivation fluid in the contraction zone 4 decreases to overcome the energy loss in the zone 4 .
- the depth of the contraction zone 4 is greater than a depth of at least a portion the channel 100 outside the contraction zone 4
- the depth of the expansion zone 6 is greater than a depth of at least a portion of the channel 100 outside the expansion zone.
- the depth of the contraction zone 4 increases leading into the entrance of the pump 5
- the depth of the expansion zone 6 decreases going away from the exit of the pump 5 .
- the algae cultivation fluid velocity is constant in the contraction zone 5
- V 1 entering the contraction zone 4 is equal or substantially equal to V 2
- the velocity V 3 of the algae cultivation fluid exiting the pump 5 is lower than the velocity V 2 entering the pump.
- the velocity V 4 exiting the expansion zone 6 is the same or substantially the same as the velocity V 3 entering the expansion zone 6 because the cross-sectional area in the expansion zone 6 is constant or substantially constant.
- the energy loss for flow in the contraction 4 and expansion 6 zones is low because the velocity is constant in each of the zones.
- the lower velocity in the contraction 4 and expansion 6 zones relative to a contraction zone or expansion zone without increasing depth as the width decrease results in lower energy losses in the systems.
- the constant or substantially constant cross-sectional area resulting from the increased depth in the contraction and expansion zones can be used with sloped or level open raceway algae cultivation systems.
- FIGS. 3 and 4 illustrate another non-limiting embodiment of an open raceway algae cultivation system of the present disclosure.
- the system of FIGS. 3 and 4 is similar to the system illustrated in FIGS. 1 and 2 , except that the rate of change in the width and depth of the contraction 4 and expansion 6 zones are non-linear.
- the system of FIGS. 3 and 4 like the system of FIG. 1 , includes a channel 100 having two conduits 1 and 2 that are fluidly coupled or connected to each other by bends 3 a , 3 b .
- the algae cultivation fluid in the channel 100 is circulated by pump 5 , which again can be a paddlewheel, propeller pump, an Archimedes screw pump, a fluid jet, or any other suitable device or structure for pumping the algae cultivation fluid in the channel 100 .
- the width of the pump 5 is less than the width of the channels 1 and 2 so that leading into an entrance of the pump 5 there is a contraction zone 4 having a width that is less than a width of the channel 100 outside of the contraction zone 4 .
- the width of contraction zone 4 decreases from the portion outside the contraction zone 4 leading into the entrance of the pump 5 .
- the width of pump 5 is also less than the conduits 1 and 2 so that going away from the exit of the pump 5 , there is an expansion zone 6 having a width greater than the width of channel 100 outside the expansion zone 6 .
- the width of expansion zone 6 increases going away from the exit of pump 5 .
- FIG. 4 is a cross-sectional view of the system of FIG. 3 taken along lines B-B.
- FIG. 4 shows sloped bottoms 11 , 12 , along with variable depth contraction 4 and expansion 6 zones.
- the surface 7 of the algae cultivation fluid entering the pump 5 , and the surface 9 of the algae cultivation fluid exiting the pump 5 is open to the air.
- the bottom 8 of the channel 100 in the contraction zone 4 , and the bottom 10 of the channel 100 in the expansion zone 6 are varied to minimize the energy losses or velocity gradients in the zones.
- the pump 5 is illustrated as a propeller pump 14 located in a pipe 13 of a barrier 12 , between the contraction zone 4 and the expansion zone 6 . It should be appreciated again, however, that pump 5 can be any suitable device or structure for increasing the algae cultivation fluid elevation from the surface 7 entering the pump 5 to the surface 9 exiting the pump 5 .
- the bottoms 11 and 12 of the channel 100 are sloped downwardly to overcome energy loss in the conduits 1 and 2 and bends 3 a and 3 b , while maintaining a substantially constant depth d 1 .
- the cross-sectional area through channel 1 , bend 3 a , channel 2 , and bend 3 b is constant or substantially constant because the width and depth are substantially constant.
- the cross-sectional area in the contraction zone 4 is constant or substantially constant for a portion of the contraction zone as the depth 8 a increases, while the width of the channel decreases.
- the cross-sectional area of pipe 13 defined as ⁇ r 2 , where r is the radius of pipe, is smaller than the cross-sectional area of the channel d 1 times the width of the channel.
- the cross-sectional rea of fluid must vary entering the pump 5 to accommodate the lower cross sectional area of the pump 5 .
- the depth 8 b of the contraction zone 4 and cross-sectional area of the fluid is varied entering the pump 5 such that the energy loss is minimized.
- the depth 10 b of the expansion zone 6 is varied exiting the pump 5 such that the energy loss is minimized.
- the depth of the expansion zone 10 a is varied to match the increase in width such that the cross-sectional area is constant or substantially constant.
- the shape of the barrier 12 is also varied to further minimize the energy loss in decreasing the cross-sectional area to enter and exit the pipe 13 .
- the velocity of the circulating algae cultivation fluid is inversely proportional to the cross-sectional area, so the velocity V 1 is constant in most of the expansion zone 6 , circulating in the channels 1 and 2 and bends 3 a and 3 b , and most of the contraction zone 4 .
- the energy loss for flow in the contraction 4 and expansion 6 zones is therefore low because the velocity is constant or substantially constant in a large portion of the zones and the shape of the bottom entering the pump 5 is varied to minimize the energy loss.
- This approach illustrated in FIG. 4 can be used with a sloped or level open raceway algae cultivation system. It should therefore be appreciated that in the system of FIGS. 3 and 4 , the depth of the contraction zone 4 is greater than a depth of at least a portion the channel 100 outside the contraction zone 4 , and the depth of the expansion zone 6 is greater than a depth of at least a portion of the channel 100 outside the expansion zone.
Abstract
Description
- This application is a continuation of U.S. patent application Ser. No. 15/590,441, filed May 9, 2017, and titled “Algae Cultivation Systems and Methods with Reduced Energy Loss,” which claims the benefit of priority to U.S. provisional application No. 62/333,717, filed on May 9, 2016, which is titled “Sumpless Sloped Raceway with Reduced Energy Loss,” the contents of each which are incorporated by reference herein and relied upon in their entirety.
- This invention was made with government support under award #DE-EE0006314 and award #DE-EE0007689, both awarded by the Department of Energy (“DOE”), and under sub-recipient #06-S140633 of prime award #W911NF-14-2-0017 awarded by the Defense Advanced Research Projects Agency (“DARPA”). The government has certain rights in the invention.
- The present disclosure relates generally to algae cultivation systems and methods, and more particularly to open raceway algae cultivation systems and methods.
- Algae cultivation has become widely recognized as a promising source of food, biofuel, chemicals, and nutraceuticals. Open algae cultivation systems have been developed for large-scale cultivation. The energy to operate a pump that circulates algae cultivation fluid or slurry is an important operating cost in these open systems. Larger open systems typically have a zone in a channel width entering the pump, and zone in a channel width exiting the pump. The bottom of the channels in these systems are typically level or gently sloped, so the speed of the algae slurry is much higher in the zones entering and exiting the pumps than the velocity in the rest of the channel. The acceleration and the high velocity both result in large energy losses. For level raceways, the energy losses are even greater than sloped systems.
- New and improved algae cultivation systems and methods are accordingly needed.
- In one aspect of the present disclosure, an open raceway algae cultivation system includes a channel configured to contain an algae cultivation fluid. The channel include a contraction zone having a width and a depth. A pump is configured to circulate the algae cultivation fluid in the channel and has an entrance and an exit. The width of the contraction zone decreases leading into the entrance of the pump, and the depth of the contraction zone is greater than a depth of at least a portion of the channel located outside of the contraction zone.
- In another aspect, an open raceway algae cultivation system includes a channel configured to contain an algae cultivation fluid. The channel including an expansion zone having a width and a depth. A pump is configured to circulate the algae cultivation fluid in the channel and includes an entrance and an exit. The width of the expansion zone increases going away from the exit of the pump and the depth of the expansion zone is greater than a depth of at least a portion of the channel located outside of the expansion zone.
- It should therefore be appreciated that is an objective of the present disclosure to reduce energy losses during the flow of algae cultivation fluid through an open raceway algae cultivation system.
-
FIG. 1 is a plan view illustrating an open raceway algae cultivation system according to one embodiment of the present disclosure. -
FIG. 2 is a cross-sectional view taken along lines A-A ofFIG. 1 . -
FIG. 3 is a plan view illustrating an open raceway algae cultivation system according to another embodiment of the present disclosure. -
FIG. 4 is a cross-sectional view taken along lines B-B ofFIG. 3 . - Referring now to the figures,
FIG. 1 illustrates one non-limiting embodiment of an open raceway algae cultivation system of the present disclosure. The system includes achannel 100 having twoconduits bends pump 5, which can be a paddlewheel, a propeller pump, an Archimedes screw pump, a fluid jet, or any other suitable structure or device for circulating or pumping the algae cultivation fluid through thechannel 100. A width ofpump 5 is less than a width of theconduits pump 5 there is acontraction zone 4 having a width that is less than a width of thechannel 100 outside of thecontraction zone 4. The reduced width ofcontraction zone 4 decreases from the portion outside thecontraction zone 4 leading into the entrance of thepump 5. The width ofpump 5 is also less than theconduits pump 5, there is anexpansion zone 6 having a width greater than the width ofchannel 100 outside theexpansion zone 6. The increased width ofexpansion zone 6 increases going away from the exit ofpump 5. When algae cultivation fluid is circulated in thechannel 100 viapump 5, the fluid exits thepump 5, flows through theexpansion zone 6, through theconduit 1, aroundbend 3 a, throughconduit 2, aroundbend 3 b, throughcontraction zone 4, and back into the entrance ofpump 5. The bottom of theconduits bends expansion zone 6 to thecontraction zone 4. -
FIG. 2 is a cross-sectional view taken along lines A-A of the system ofFIG. 1 illustrating a level bottom, variabledepth contraction zone 4, and a variabledepth expansion zone 6. Thesurface 7 of the algae cultivation fluid entering the pumping, and the surface 9 of the fluid exiting thepump 5 is open to the air. Abottom 8 of thechannel 100 in thecontraction zone 4, and abottom 10 of thechannel 100 in theexpansion zone 6 are sloped downwardly toward thepump 5 to maintain a substantially constant cross-sectional area. Thepump 5 is illustrated as a paddlewheel, but the pump can be any device or structure suitable for increasing the algae cultivation fluid elevation from thesurface 7 of the fluid entering thepump 5 to the surface 9 of the fluid exiting thepump 5. When the algae cultivation fluid is circulating in thechannel 100, the depth d3 of fluid exiting thepump 5 is the greatest, while the depth of the fluid going away from the exit of thepump 5 decreases to d4 so as to maintain a constant cross-sectional area of the algae cultivation fluid throughout theexpansion zone 6. In an embodiment, the cross-sectional area of the algae cultivation fluid in thechannel 100 can be defined as the depth of the algae fluid depth times a width of thechannel 100. The elevation of the surface 9 of the algae cultivation fluid decreases in theexpansion zone 6 to overcome energy loss in thezone 6. The algae cultivation fluid depth decreases from depth d4 to depth d1 to overcome energy loss in thechannels contraction zone 4 as the fluid leads into the entry of thepump 5 so as to maintain a substantially constant cross-sectional area in thecontraction zone 4. The elevation of thesurface 7 of the algae cultivation fluid in thecontraction zone 4 decreases to overcome the energy loss in thezone 4. It should therefore be appreciated that in the system ofFIGS. 1 and 2 , the depth of thecontraction zone 4 is greater than a depth of at least a portion thechannel 100 outside thecontraction zone 4, and the depth of theexpansion zone 6 is greater than a depth of at least a portion of thechannel 100 outside the expansion zone. It should likewise be appreciated that in the system ofFIGS. 1 and 2 , the depth of thecontraction zone 4 increases leading into the entrance of thepump 5, and the depth of theexpansion zone 6 decreases going away from the exit of thepump 5. - Because the cross-sectional area of the algae cultivation fluid is constant in the
contraction zone 4, the algae cultivation fluid velocity is constant in thecontraction zone 5, and V1 entering thecontraction zone 4 is equal or substantially equal to V2. The velocity V3 of the algae cultivation fluid exiting thepump 5 is lower than the velocity V2 entering the pump. The velocity V4 exiting theexpansion zone 6 is the same or substantially the same as the velocity V3 entering theexpansion zone 6 because the cross-sectional area in theexpansion zone 6 is constant or substantially constant. The energy loss for flow in thecontraction 4 andexpansion 6 zones is low because the velocity is constant in each of the zones. Furthermore, the lower velocity in thecontraction 4 andexpansion 6 zones relative to a contraction zone or expansion zone without increasing depth as the width decrease results in lower energy losses in the systems. The constant or substantially constant cross-sectional area resulting from the increased depth in the contraction and expansion zones can be used with sloped or level open raceway algae cultivation systems. -
FIGS. 3 and 4 illustrate another non-limiting embodiment of an open raceway algae cultivation system of the present disclosure. The system ofFIGS. 3 and 4 is similar to the system illustrated inFIGS. 1 and 2 , except that the rate of change in the width and depth of thecontraction 4 andexpansion 6 zones are non-linear. The system ofFIGS. 3 and 4 , like the system ofFIG. 1 , includes achannel 100 having twoconduits bends channel 100 is circulated bypump 5, which again can be a paddlewheel, propeller pump, an Archimedes screw pump, a fluid jet, or any other suitable device or structure for pumping the algae cultivation fluid in thechannel 100. The width of thepump 5 is less than the width of thechannels pump 5 there is acontraction zone 4 having a width that is less than a width of thechannel 100 outside of thecontraction zone 4. The width ofcontraction zone 4 decreases from the portion outside thecontraction zone 4 leading into the entrance of thepump 5. The width ofpump 5 is also less than theconduits pump 5, there is anexpansion zone 6 having a width greater than the width ofchannel 100 outside theexpansion zone 6. The width ofexpansion zone 6 increases going away from the exit ofpump 5. When algae cultivation fluid is circulated in thechannel 100 viapump 5, the fluid exits thepump 5, flows through theexpansion zone 6, through theconduit 1, aroundbend 3 a, throughconduit 2, aroundbend 3 b, throughcontraction zone 4, and back into the entrance ofpump 5. The bottom of theconduits bends expansion zone 6 to thecontraction zone 4. - Referring more specifically to
FIG. 4 ,FIG. 4 is a cross-sectional view of the system ofFIG. 3 taken along lines B-B.FIG. 4 shows slopedbottoms variable depth contraction 4 andexpansion 6 zones. Thesurface 7 of the algae cultivation fluid entering thepump 5, and the surface 9 of the algae cultivation fluid exiting thepump 5 is open to the air. Thebottom 8 of thechannel 100 in thecontraction zone 4, and the bottom 10 of thechannel 100 in theexpansion zone 6 are varied to minimize the energy losses or velocity gradients in the zones. Thepump 5 is illustrated as apropeller pump 14 located in apipe 13 of abarrier 12, between thecontraction zone 4 and theexpansion zone 6. It should be appreciated again, however, thatpump 5 can be any suitable device or structure for increasing the algae cultivation fluid elevation from thesurface 7 entering thepump 5 to the surface 9 exiting thepump 5. - The
bottoms channel 100 are sloped downwardly to overcome energy loss in theconduits channel 1, bend 3 a,channel 2, andbend 3 b is constant or substantially constant because the width and depth are substantially constant. The cross-sectional area in thecontraction zone 4 is constant or substantially constant for a portion of the contraction zone as thedepth 8 a increases, while the width of the channel decreases. The cross-sectional area ofpipe 13, defined as πr2, where r is the radius of pipe, is smaller than the cross-sectional area of the channel d1 times the width of the channel. The cross-sectional rea of fluid must vary entering thepump 5 to accommodate the lower cross sectional area of thepump 5. Thedepth 8 b of thecontraction zone 4 and cross-sectional area of the fluid is varied entering thepump 5 such that the energy loss is minimized. Similarly, thedepth 10 b of theexpansion zone 6 is varied exiting thepump 5 such that the energy loss is minimized. The depth of theexpansion zone 10 a is varied to match the increase in width such that the cross-sectional area is constant or substantially constant. The shape of thebarrier 12 is also varied to further minimize the energy loss in decreasing the cross-sectional area to enter and exit thepipe 13. The velocity of the circulating algae cultivation fluid is inversely proportional to the cross-sectional area, so the velocity V1 is constant in most of theexpansion zone 6, circulating in thechannels contraction zone 4. The energy loss for flow in thecontraction 4 andexpansion 6 zones is therefore low because the velocity is constant or substantially constant in a large portion of the zones and the shape of the bottom entering thepump 5 is varied to minimize the energy loss. This approach illustrated inFIG. 4 can be used with a sloped or level open raceway algae cultivation system. It should therefore be appreciated that in the system ofFIGS. 3 and 4 , the depth of thecontraction zone 4 is greater than a depth of at least a portion thechannel 100 outside thecontraction zone 4, and the depth of theexpansion zone 6 is greater than a depth of at least a portion of thechannel 100 outside the expansion zone.
Claims (18)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US16/988,149 US20200367458A1 (en) | 2016-05-09 | 2020-08-07 | Algae cultivation systems and methods with reduced energy loss |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201662333717P | 2016-05-09 | 2016-05-09 | |
US15/590,441 US10772272B2 (en) | 2016-05-09 | 2017-05-09 | Algae cultivation systems and methods with reduced energy loss |
US16/988,149 US20200367458A1 (en) | 2016-05-09 | 2020-08-07 | Algae cultivation systems and methods with reduced energy loss |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US15/590,441 Continuation US10772272B2 (en) | 2016-05-09 | 2017-05-09 | Algae cultivation systems and methods with reduced energy loss |
Publications (1)
Publication Number | Publication Date |
---|---|
US20200367458A1 true US20200367458A1 (en) | 2020-11-26 |
Family
ID=60242364
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US15/590,441 Active 2037-11-08 US10772272B2 (en) | 2016-05-09 | 2017-05-09 | Algae cultivation systems and methods with reduced energy loss |
US16/988,149 Abandoned US20200367458A1 (en) | 2016-05-09 | 2020-08-07 | Algae cultivation systems and methods with reduced energy loss |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US15/590,441 Active 2037-11-08 US10772272B2 (en) | 2016-05-09 | 2017-05-09 | Algae cultivation systems and methods with reduced energy loss |
Country Status (1)
Country | Link |
---|---|
US (2) | US10772272B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP6736067B1 (en) * | 2019-04-19 | 2020-08-05 | 株式会社日鰻 | Algae growing device |
Family Cites Families (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2732662A (en) | 1956-01-31 | Mass culture of algae | ||
US3243918A (en) | 1963-03-13 | 1966-04-05 | Robert A Erkins | Method for propagating photosynthetic microorganisms |
US4320594A (en) | 1978-12-28 | 1982-03-23 | Battelle Memorial Institute | Mass algal culture system |
US4253271A (en) | 1978-12-28 | 1981-03-03 | Battelle Memorial Institute | Mass algal culture system |
CZ326696A3 (en) | 1996-11-06 | 1998-05-13 | Mikrobiologický Ústav Av Čr | Process of external thin-layer cultivation of algae and blue-green algae and a bioreactor for making the same |
US20110229775A1 (en) | 2008-09-22 | 2011-09-22 | Phycosystems, Inc. | Device for Efficient, Cost-Effective Conversion of Aquatic Biomass to Fuels and Electricity |
US8769867B2 (en) | 2009-06-16 | 2014-07-08 | Aurora Algae, Inc. | Systems, methods, and media for circulating fluid in an algae cultivation pond |
WO2010151837A2 (en) | 2009-06-26 | 2010-12-29 | The Arizona Board Of Regents On Behalf Of The University Of Arizona | Aquaculture raceway integrated design |
MY159248A (en) | 2009-07-28 | 2016-12-30 | Joule Unlimited Tech Inc | Photobioreactors, solar energy gathering systems, and thermal control methods |
NO330205B1 (en) | 2009-09-09 | 2011-03-07 | Microa As | photobioreactor |
US20110287531A1 (en) | 2010-05-20 | 2011-11-24 | Hazlebeck David A | Microalgae Growth Pond Design |
MX2013009620A (en) | 2011-02-25 | 2014-05-27 | Algenol Biofuels Inc | Magnetically coupled system for mixing. |
US8752329B2 (en) * | 2011-04-29 | 2014-06-17 | Aurora Algae, Inc. | Optimization of circulation of fluid in an algae cultivation pond |
US8541225B2 (en) | 2011-07-25 | 2013-09-24 | General Atomics | System and method for using a pulse flow circulation for algae cultivation |
US9295206B2 (en) * | 2012-04-12 | 2016-03-29 | Johna Ltd | Method of culturing algae |
GB2501101B (en) * | 2012-04-12 | 2014-06-11 | Seagrass Ag Sa Ltd | Method of culturing algae |
WO2013186626A1 (en) | 2012-06-12 | 2013-12-19 | Arvind Mallinath Lali | Raceway pond system for increased biomass productivity |
EP2875724B1 (en) * | 2013-11-25 | 2016-01-06 | FCC Aqualia, S.A. | Open reactor for cultivating microalgae |
US20150182923A1 (en) | 2013-12-31 | 2015-07-02 | Algenol Biofuels Inc. | Liquid Agitation System, Kit And Method Of Use |
AU2017262679B2 (en) * | 2016-05-09 | 2022-04-07 | Global Algae Technology, LLC | Algae cultivation systems and methods with bore waves |
-
2017
- 2017-05-09 US US15/590,441 patent/US10772272B2/en active Active
-
2020
- 2020-08-07 US US16/988,149 patent/US20200367458A1/en not_active Abandoned
Also Published As
Publication number | Publication date |
---|---|
US20170318764A1 (en) | 2017-11-09 |
US10772272B2 (en) | 2020-09-15 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US11639811B2 (en) | Apparatus including a clean mini environment | |
US8752329B2 (en) | Optimization of circulation of fluid in an algae cultivation pond | |
US20200367458A1 (en) | Algae cultivation systems and methods with reduced energy loss | |
US11512689B2 (en) | Undulating-membrane fluid circulator | |
CN106461145B (en) | Commutate elbow | |
BR112016002731A2 (en) | elastomeric emitter and related methods | |
MX2016013665A (en) | Pump drive unit for conveying a process fluid. | |
JP6762724B2 (en) | Piping of driven fluid machinery | |
EP3290324A1 (en) | Dual cavity air lubrication system | |
EP3183487B1 (en) | Fluid transport pipe | |
US20170268523A1 (en) | Floating-bearing motor pump cooled by a circulating fluid | |
US10760672B2 (en) | Coolant system pressure drop reduction | |
US11491450B2 (en) | Cavitation reactor | |
US20170027120A1 (en) | Low flow pond for algae cultivation | |
US9845980B2 (en) | Air conditioning system with evaporative cooling system | |
BR102020022903A8 (en) | Subsea installation for heating a liquid/gas diphase effluent that circulates within a submarine casing | |
RU2688873C1 (en) | Centrifugal pump stage | |
US4253964A (en) | Device for bringing about particle growth in a flowing liquid suspension | |
US9840822B2 (en) | Drain assisting water fixture | |
US11186383B2 (en) | Centrifugal fuel pump ice prevention | |
RU2577919C1 (en) | Impeller pump | |
US1361938A (en) | Centrifugal pump | |
CN208764536U (en) | Commutate elbow | |
KR20230001352U (en) | thermal management system | |
Ivanyushin et al. | Replaceable Hydraulic Parts in Spiral Volute Pumps |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AS | Assignment |
Owner name: GLOBAL ALGAE INNOVATIONS, INC., CALIFORNIA Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:HAZLEBECK, DAVID A.;REEL/FRAME:053559/0180 Effective date: 20170508 Owner name: GLOBAL ALGAE TECHNOLOGIES, LLC, CALIFORNIA Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:GLOBAL ALGAE INNOVATIONS, INC.;REEL/FRAME:053559/0208 Effective date: 20190603 |
|
AS | Assignment |
Owner name: UNITED STATES DEPARTMENT OF ENERGY, DISTRICT OF COLUMBIA Free format text: CONFIRMATORY LICENSE;ASSIGNOR:GLOBAL ALGAE INNOVATIONS, INC.;REEL/FRAME:053972/0184 Effective date: 20200831 |
|
STPP | Information on status: patent application and granting procedure in general |
Free format text: DOCKETED NEW CASE - READY FOR EXAMINATION |
|
AS | Assignment |
Owner name: GLOBAL ALGAE TECHNOLOGY, LLC, CALIFORNIA Free format text: CORRECTIVE ASSIGNMENT TO CORRECT THE ASSIGNEE NAME PREVIOUSLY RECORDED AT REEL: 053559 FRAME: 0208. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT;ASSIGNOR:GLOBAL ALGAE INNOVATIONS, INC.;REEL/FRAME:055313/0601 Effective date: 20210208 |
|
STPP | Information on status: patent application and granting procedure in general |
Free format text: NON FINAL ACTION MAILED |
|
STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |