NO20140975A1 - Bioreactor and process for microalgae production - Google Patents

Bioreactor and process for microalgae production Download PDF

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Publication number
NO20140975A1
NO20140975A1 NO20140975A NO20140975A NO20140975A1 NO 20140975 A1 NO20140975 A1 NO 20140975A1 NO 20140975 A NO20140975 A NO 20140975A NO 20140975 A NO20140975 A NO 20140975A NO 20140975 A1 NO20140975 A1 NO 20140975A1
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reactor
harvesting
algae
following
production
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NO20140975A
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Norwegian (no)
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Jan Erik Kyrkjebø
Jan Fredrik Garvik
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Biosystems As
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Priority to EP15818508.2A priority Critical patent/EP3167043B1/en
Priority to PCT/NO2015/050125 priority patent/WO2016007016A1/en
Priority to CN201580042578.6A priority patent/CN107155333B/en
Priority to NO20150893A priority patent/NO340051B1/en
Priority to US15/324,420 priority patent/US20170158995A1/en
Priority to JP2017522310A priority patent/JP6621817B2/en
Publication of NO20140975A1 publication Critical patent/NO20140975A1/en

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Description

Innledning og beskrivelse. Introduction and description.

Denne patentsøknaden er en videre forbedret innretning for en mer effektiv algeproduksjon enn utførelseseksemplene beskrevet i patentsøknad 20140866 av 2014-07-08. This patent application is a further improved device for more efficient algae production than the design examples described in patent application 20140866 of 2014-07-08.

Det er kjent en rekke systemer og anordinger for produksjon av mikroalger i reaktorer, slik som raceways anlegg hvor selve algeproduksjonen foregår samt en separat innretning for innhøsting av algene. A number of systems and devices are known for the production of microalgae in reactors, such as raceway facilities where the actual algae production takes place as well as a separate device for harvesting the algae.

Disse systemen krever særdeles store arealer og og blir svært kostbare. Videre vil de være særdeles dyre i å holde i drift pga reingjøring og vedlikehold. These systems require particularly large areas and are very expensive. Furthermore, they will be extremely expensive to keep in operation due to cleaning and maintenance.

De blir svært så kompliserte i oppbygging og lite effektive . They become very complicated in structure and not very effective.

I tillegg vil det bli utsatt for forurensinger og vil som regel bli bygget på steder med dårlig infrastruktur og i tilknytting til røkgassanlegg der man tar ut C02 som i tillegg til lys er en betingelse for art mikrolager skal vokse i antall. In addition, it will be exposed to pollution and will, as a rule, be built in places with poor infrastructure and in connection with flue gas plants where C02 is taken out, which, in addition to light, is a condition for species of microstorage to grow in number.

Med den foreliggende oppfinnelsen tar man sikte på å løse dagens kmpliserte og kostbare innretninger og samtidig få et lukket system der man bruker effektivt sjøvann som C02-kilde og der man i tillegg får oppnår å få et lukket produksjons og innhøstingsanlegg i en og samme eneheten. With the present invention, the aim is to solve today's complicated and expensive devices and at the same time get a closed system where you use seawater effectively as a C02 source and where you also achieve a closed production and harvesting facility in one and the same unit.

Det tas sikte på å kombinere algeproduksjonen og innhøstingen i en og samme enheten. The aim is to combine algae production and harvesting in one and the same unit.

I tillegg tar man sikte på å lukke reaktoren inn med et lukket rom i glassmatrialet eller som trenger inn lys og samtidig unngår forurensninger utenfra og som har et kompakt volum med lave byggemål. In addition, the aim is to enclose the reactor with a closed space in the glass material or which penetrates light and at the same time avoids contamination from the outside and which has a compact volume with low construction dimensions.

Dette gjør at man vil kunne levere algeoljer og produktet til et utvidet marked slik som til kosmetisk , forproduksjon til oppdrett og tii farmasøytisk industri. This means that it will be possible to supply algae oils and the product to an expanded market such as for cosmetics, pre-production for farming and in the pharmaceutical industry.

I tillegg tar man sikte på å utnutte avfall fra oppdrettsanlegg på en enkel måte og samtidig som det kan utvinnes komprimert oksygen fra algeproduksjonen. In addition, the aim is to utilize waste from aquaculture facilities in a simple way and at the same time compressed oxygen can be extracted from algae production.

Dette kan løses ved at reaktorlikket er tett, men at man sørger for in utnyttelse av den oksygen som utskiller fra lageproduksjonen. Dette kan skje ved at huset eller lokket er tilsuttet en vifte med et lukket rørsystem i stedenfor å sleppe oksygen ut i atmosfæren. This can be solved by keeping the reactor leak tight, but making sure that the oxygen released from the batch production is utilized. This can happen because the housing or lid is connected to a fan with a closed pipe system instead of releasing oxygen into the atmosphere.

Man kan da bringe oksygen i til f-eks. en generator og /eller kompressor som komprimerer oksygengassen direkte og som gjør det mulig i lagre dette fortløpende på flasker og som et komplett oksygenfalsebatteri, og som igjen kan være et ytterligere salgbart produkt til oppdrettsnæringen og ellers til ønskede formål knyttet opp ot oskygen på fasker. One can then bring in oxygen to e.g. a generator and/or compressor which compresses the oxygen gas directly and which makes it possible to store this continuously in bottles and as a complete oxygen storage battery, and which in turn can be an additional salable product for the farming industry and for other desired purposes linked to the oxygen in the fish tank.

Dette gjør i flg oppfinnelsen til både en svært effektiv produksjon og ved at man oppnår et ekstra produkt i form av oksygen ferdig produsert og leveringsklart fra selve reaktorenhetene. This, in turn, makes the invention both a very efficient production and by obtaining an additional product in the form of oxygen ready-made and ready for delivery from the reactor units themselves.

Dette vil være en styrke og være ne stor resurs som oppdrettsnæringen bruker i forbindelse med avlusning, invasjon av maneter i oppddrettsamnleggen og som tilsetning og back up for lukkete og landbaserte oppdrettsanlegg. This will be a strength and be a great resource that the farming industry uses in connection with de-lice, invasion of jellyfish in the farming community and as an addition and back up for closed and land-based farming facilities.

Videre kan i flg oppfinnelsen det sikres en høyere temperatur i algereaktoren og i algeproduksjonen, slik som basis algekulturtanker som også kan installeres på reaktorenheten og til oppvarming av algekulturen . Dette kan gjøres ved at f.eks at varmen som blir utviklet fra komprimeringen av oksygengassen blir varmevekslet med sjøvannet som tas inn i reaktoren og som da også tjener som kjøling av selve oksygenproduksjonen. Furthermore, according to the invention, a higher temperature can be ensured in the algae reactor and in the algae production, such as basic algae culture tanks that can also be installed on the reactor unit and for heating the algae culture. This can be done by, for example, the heat developed from the compression of the oxygen gas being heat exchanged with the seawater that is taken into the reactor and which then also serves as cooling for the oxygen production itself.

Det tas sikte på en teknisk løsning som gir god kontroll, lave investeringskostnader og en effektiv og kompakt og vedlikeholdsvennlig utførelse av algeproduksjonen samt en fremgangsmåte for algeproduksjon og innhøsting som er mer kontinuerlig, hygienisk og effektiv enn det som er kjent med dagens løsninger. The aim is a technical solution that provides good control, low investment costs and an efficient, compact and maintenance-friendly execution of algae production, as well as a method for algae production and harvesting that is more continuous, hygienic and efficient than what is known with today's solutions.

Videre vil løsningen i hht oppfinnelsen skikre at alle brannforskrifter enkelt kan tilfredsstilles samtidg som man etterstreber å få en egonomisk funksjonell løsning for kontroll av selve algeproduksjonene og prosessen rundt denne. Furthermore, the solution according to the invention will ensure that all fire regulations can be easily satisfied at the same time as striving for an ergonomically functional solution for controlling the algae production itself and the process surrounding it.

Ytterligere er det i flg oppfinnelsen er det en vesentlig fordel at innhøstingsrenne er så som mulif i yrrekant der algebiomassen kan skli utover perifert og ut av reaktoren ved at renna er svakt hellende og kones innover mot et hjørne eller et avløp i tilknytting til awanningsenheter i form av en dekanter,sentruivfuge og eventulet også en presse for ytterligere å kunne separere ut ren algolje som er mettet omega 3 syre og som har en høyere pris enn selve algebiomassen. Furthermore, according to the invention, it is a significant advantage that the harvesting chute is like a mulif at the udder edge where the algal biomass can slide outward peripherally and out of the reactor by the chute being slightly inclined and tapering inwards towards a corner or a drain in connection with dewatering units in the form of a decanter, centrifuge joint and possibly also a press to be able to further separate out pure algal oil which is saturated with omega 3 acid and which has a higher price than the algal biomass itself.

Algebiomassen kan ytterligere anvendes som jetfuel og dyrefor. The algae biomass can further be used as jet fuel and animal feed.

Fremgansmåte for produksjon av mikroalger. Process for the production of microalgae.

Det er vist en fremgangsmåte for produksjon,innhøsting og lagring av algeproduktene produsert i reaktoren. A method for the production, harvesting and storage of the algal products produced in the reactor is shown.

Det henvises til utførelseseksmpel i hht vedlagte figurer. Reference is made to the design example in relation to the attached figures.

Dene løsningen har sitt utspring fra patentsøknad «Bioreaktor» innlevert patentsøknad nr. 210140866 av 2014-07-08. These solutions originate from the patent application "Bioreaktor" filed patent application no. 210140866 of 2014-07-08.

Det vist en Bioreaktorenhet 1 som flyter ved hjelp av et oppdriftslegeme 2 med kai 16 og som kan ankres opp i sjøen permanent via forankringsliner 5. Det er vist et flytelegeme eller flytekrage eller opptriftsflåte 2 som holder hele algeprodukksjonsanlegget flytende og der er vist et lukket hus 3 som slipper igjennom lys.ira atmosfæren 58.1 tillegg til at det kan tilsettes kunstig lys i bunn og begger 47a,47b i rektorbassenget 1. ler det ist et antall blandegrinder 45 og høstegrind 48 som er opplagret i senter av reaktoren 1 via et ett lager 62 og en elektrisk slepring 95 som skaloverføre elektrisk strøm til grindene 45,48 samt at det lukkete lageret 62 fordeler vannstrømmen 33 sammensatt av midler 34,33. og 81 tilgnndene 45,48. A Bioreactor unit 1 is shown which floats with the help of a buoyancy body 2 with a quay 16 and which can be permanently anchored in the sea via anchoring lines 5. A floating body or buoyancy collar or buoyancy raft 2 is shown which keeps the entire algae production facility afloat and a closed house is shown 3 which lets light through into the atmosphere 58.1 in addition to the fact that artificial light can be added to the bottom and both sides 47a, 47b in the rector basin 1. There is also a number of mixing gates 45 and harvesting gates 48 which are stored in the center of the reactor 1 via a single warehouse 62 and an electric slip ring 95 which will transmit electric current to the gates 45,48 and that the closed bearing 62 distributes the water flow 33 composed of means 34,33. and 81 grants 45.48.

Det er vist gangbroer 53 og kontrollrom 80a som sikrer en oversiktlig og ergonomisk drift av algeanlegget eller bioreaktorenheten 1. Footbridges 53 and control room 80a are shown, which ensure clear and ergonomic operation of the algae plant or bioreactor unit 1.

Ved at det gjennomsiktig husets tak 3 er montert så lavt som mulig og fortrinnsvis i nivå under gangbro53 og kontrollrom 80a, gjør dette løsningen i flg oppfinnelsen svært lavt flytende i sjøen 61, som igjen er en fordel rent estetisk samt en betydelig billiigere løsning i tillegg til at produksjonen skjer på en miljøvennlig og rein måte. Ytterligere kreves det mindre vdelikehold med dette utførselseseksemplet. By the fact that the transparent roof 3 of the house is mounted as low as possible and preferably at a level below the footbridge 53 and control room 80a, this makes the solution according to the invention very low floating in the sea 61, which again is a purely aesthetic advantage as well as a significantly cheaper solution in addition to ensure that production takes place in an environmentally friendly and clean manner. Furthermore, less maintenance is required with this export example.

Ytterligere utsettesdette utførelseseksempelet eller reaktoren 1 for mindre vindkrefter som kan forenkle forankringen 5 av denne og utvide området hvor produksjonen kan foregå. Furthermore, this design example or the reactor 1 is exposed to minor wind forces which can simplify the anchoring 5 of this and expand the area where production can take place.

Det er vist et kontrollrom 80a og et maskinrom 80c der kontrollrom 80a og grinder 45,48 er opplagret i lagerpakken 62 . Dette gjør konstruksjonen svært enkel å bygge ved at lagerpakken har en svært liten diameter og at grindene 45,48 er støttet og blir drevet rundt i en kontrollert hastighjet vmed gearmotorene 55 plassert på reaktorens dekk 16 godt innenfor huset 3 vegger. A control room 80a and a machine room 80c are shown where control room 80a and grinders 45,48 are stored in the storage package 62. This makes the construction very easy to build in that the bearing package has a very small diameter and that the gates 45,48 are supported and are driven around at a controlled speed with the gear motors 55 placed on the reactor deck 16 well inside the house 3 walls.

Lagerpakken er dermed opphengt i gangbroene 53 og som blir da blir en svært stiv og robust konstruksjon. The storage package is thus suspended in the footbridges 53 and which then becomes a very rigid and robust construction.

Et antall algeblaned-grinder 45 og innhøstingsgrinder 48 kan roteres rundt senterlageret 62 og som er innrettet til å kunne styres i en retning for blanding ,innpumping av basis-algekultur, ekstra belysning og der blandegrinedene 45 kan være er opplagret over en innhøstingsgrinden 48 og at grindene 45,48 i tillegg til å kunne kjøres rundt i ring ved hjelp av gearmotorene 55, kan vippes opp når det kun produseres og tilsavrende under vedlikehold.kan vippes opp av algekulturen for vedlikehold og slik at blandegrindene 45 kan bevege seg under selv innhøstingsgrinden 48 under algeproduksjon. A number of algae mixing grates 45 and harvesting grates 48 can be rotated around the central bearing 62 and which are arranged to be able to be controlled in a direction for mixing, pumping in basic algae culture, additional lighting and where the mixing grates 45 can be stored above a harvesting grate 48 and that the gates 45,48, in addition to being able to be driven around in a ring with the help of the gear motors 55, can be tilted up when it is only being produced and added during maintenance. can be tilted up by the algae culture for maintenance and so that the mixing gates 45 can move under the harvesting gate 48 itself during algae production.

Det er vist 2 oppovervendte bunner 92a,92b med en innhøstingsrenne 42 på øverste punkt i overflatesonen som skrår eller heller svakt utover mot periferien og kaien 2,16. 2 upward facing bottoms 92a, 92b are shown with a harvesting chute 42 at the top point in the surface zone which slopes or rather slightly outwards towards the periphery and the quay 2, 16.

På denne måten kan oppnås en svært fleksibel og effektiv produksjon og innhøsting av algebiomassen i en og samme enhet. Ytterligere effektiv blir innhøøstingen ved at renna 42 er svakt hellende utover og nedover i pontongen 2 under dekk 16 og at renna yderretter er vinklet innover mot innsigsiden av ytterligere midler 38,86. På denne måten kan algebiomassen le renner fritt nedover fra senter og ut og fritt nedover i den koniske oppsamlingstanken 36 som igjen står i tilknytning til en pumpe og/eller sentrifugeog/ eller dekanter 38, og/eller en presse 86 og som da ytterligere avvanner algebiomassen le og samtidg sepparere ut ren algeolje lf som kan lagres i en nedsenkbar tank 18 og samtidg produsere algerestbiomasse lg som kan transporters til og lagres i en tank 91b via en ledning 91a. Dette kan i og for seg være en pumpeledning for strømning eller være en transportskrue.Overskuddsbiomasse kan ytterligere pumpes i retur til reaktoren 1 via ledningene 39,89 for å brukes på nytt i algeproduksjonen. In this way, a very flexible and efficient production and harvesting of the algae biomass can be achieved in one and the same unit. The harvesting is made even more efficient by the fact that the chute 42 is slightly inclined outwards and downwards in the pontoon 2 below the deck 16 and that the outer right of the chute is angled inwards towards the inlet side by additional means 38,86. In this way, the algal biomass can flow freely downwards from the center out and freely downwards into the conical collection tank 36 which is in turn connected to a pump and/or centrifuge and/or decanter 38, and/or a press 86 and which then further dewaters the algal biomass le and simultaneously separate out pure algal oil lf which can be stored in a submersible tank 18 and simultaneously produce algal residue biomass lg which can be transported to and stored in a tank 91b via a line 91a. This can in and of itself be a pump line for flow or be a transport screw. Surplus biomass can further be pumped back to the reactor 1 via the lines 39,89 to be used again in algae production.

På denne måten kan det produseres et ette rt a kt et produkt i form av algeplje som er høyere priset og der produksjonen blir særdeles effektiv der ikke noe algekultur går til spille. In this way, a product can be produced in the form of algae treatment which is priced higher and where production is extremely efficient where no algae culture is wasted.

På denne måten oppnår man en kontinuerlig og fleksibel produksjon og innhøsting og som kan automatsieres og styres kontrollert og kontinuerlig i form av en delvis rykkvis bevegelse eller at grinddene 45, kan stå stille en viss tid inntill algeproduksjonen er stor nok til innhøsting og der innhøstingen da kan automatsieres i tillegg ved at at ved at både blandegrinder 45 og innhøstingsgrindener 48 også kan styres i en retning og vippes opp fra reaktoren 1. In this way, a continuous and flexible production and harvesting is achieved and which can be automated and controlled in a controlled and continuous manner in the form of a partially jerky movement or that the gates 45 can stand still for a certain time until the algae production is large enough for harvesting and where the harvesting then can also be automated in that both mixing grates 45 and harvesting grates 48 can also be controlled in one direction and tilted up from the reactor 1.

Etter behov kan i følge oppfinnelsen innhøstingsgrindene dermed vippes opp og senkes ned alt etter som for videre produksjon samtidig som renna tømmer seg for alger og samtidig som algeproduksjonen er intensive ved at blandegrindne 45 fremdeles er i full funksjon. As needed, according to the invention, the harvesting gates can thus be tilted up and lowered as needed for further production at the same time as the chute is emptied of algae and at the same time as the algae production is intensive in that the mixing gates 45 are still in full function.

Ytterligere er innhøstingrindene 48 hengslet slik at grindene slepes langsbunn 47a og vegger 47b som igjen rengjør alle overflater ved hjelp av kostene 60 innrettet i ytterkant av grindene 45 og/eller 48 og dermed utgjøre en mer eller mindre vedlikeholdsfri løsning. Furthermore, the harvest gates 48 are hinged so that the gates are dragged along the bottom 47a and walls 47b, which in turn cleans all surfaces with the help of the brooms 60 arranged at the outer edge of the gates 45 and/or 48 and thus constitute a more or less maintenance-free solution.

På denne måten kan produksjonen skje både dag og natt på en mer eller mindre helautoatisk prosess og ved at selve reaktorbassenget 1 ikke trengs tappes ned eller rengjøres manuelt. In this way, production can take place both day and night in a more or less fully automatic process and in that the reactor basin 1 itself does not need to be drained or cleaned manually.

Fra algeproduksjonen i den lukkete reaktorens 1 hus 3 blir det utskilt oksygengass 7a. På fig. I a.lb,lc,ld, 2og 3 er det vist vist en vifte 9 og et sugerørsystem 7 som suger utskilt oksygengass 7a fra rommet 58 bioreaktoren 1. omsluttet av huset 3 inn i en kompressor og eventuelt via en oksygengenerator 8c og so komprimerer den frie oksygenen 87 til høyt trykk og som kan lagres i en trykktank 87b for senere påfylling i gassflasker 85 som igjen kan brukes til oksygen for f. eks.oppdrettsanlegg langs kysten. Kompressoren 87a kan være omsluttet av en kjøler 4b hvis kjølevann er koblet til sjøvannsintaksledningen 4 og som dermed sørger for at sjøvannet som blir pumpet inn i reaktoren 1 aldri blir underlkjølt som igjen kan skade verdien på algeproduksjone ved at oljen 1 f harskner eller forringes i verdi. From the algae production in the closed reactor 1 housing 3, oxygen gas 7a is released. In fig. In a.lb,lc,ld, 2 and 3, a fan 9 and a suction pipe system 7 are shown which suck secreted oxygen gas 7a from the room 58 the bioreactor 1. enclosed by the housing 3 into a compressor and possibly via an oxygen generator 8c and so compresses the free oxygen 87 to high pressure and which can be stored in a pressure tank 87b for later filling in gas cylinders 85 which can again be used for oxygen for e.g. breeding facilities along the coast. The compressor 87a can be enclosed by a cooler 4b whose cooling water is connected to the seawater intake line 4 and which thus ensures that the seawater that is pumped into the reactor 1 is never subcooled, which in turn can damage the value of algae production by causing the oil 1f to go rancid or deteriorate in value .

På denne måten kan man oppnå både en produksjon og magasinering av komprimert oksygen og varme opp sjøvannet som hindrer algebiomassen lf, oljen 17 eller biomassen 91 å forringes i verdi pga underkjøling. In this way, one can achieve both a production and storage of compressed oxygen and heat the seawater, which prevents the algal biomass 1f, the oil 17 or the biomass 91 from deteriorating in value due to subcooling.

Dette sikrer kalitetssikre algeprodukter som dermed får en vedlig bred anvendelse og et stort marked og der kvaliteten på produktene gjør at man kan ta en høyere pris ut i markedet. This ensures quality-safe algae products, which thus get a wide range of use and a large market, and where the quality of the products means that you can charge a higher price on the market.

Det er vist et tak 3 eller lokk i glass 3 i gjennomsiktig matriale og som kan være utsyrt med A roof 3 or lid in glass 3 in transparent material is shown and which can be equipped with

avluftingsluker 3b i tilfellet utsigingsviftene stopper eller det oppstår for høyt oksygennivå i forhold til myndighetenes krav. Da kan disse lukene være hengslet og kunne åpnes automatisk ved en vrimotor som åpner vinduene 3b autmatisk ved for høye oksygennivåer. Dette sikrer en eksplosjonsfri reaktor som dermed kan få en generall godkjennelse mht eksplosjonnssikkerhet. Viften 9 kan være elektrisk drebe\ver av en motor 9a som via en akskling står i åpne atmosfære. Dette sikrer reaktoren 1 ytterligere mot eksplosjonsfare. ventilation hatches 3b in the event that the extraction fans stop or the oxygen level is too high in relation to the authorities' requirements. Then these hatches can be hinged and can be opened automatically by a turning motor which opens the windows 3b automatically in case of too high oxygen levels. This ensures an explosion-free reactor which can thus receive a general approval in terms of explosion safety. The fan 9 can be electrically driven by a motor 9a which is in the open atmosphere via a shaft. This further secures the reactor 1 against the risk of explosion.

Videre er det vist ytterligere trekk på fig. 4a,4b,5a,5b,6,7a,7b og 8a,8b hvor gindene 45,48 kan være Forbundet med et rør eller rammeverk 99, hvor det er festet kunstig lys f.eks.i form av stang eller rørlys 98 som kan henges opp i rammeverket 99 i hensiktmessige innbyrdes avstander og som da kan roteres med blandegindene 45 og sørge for ytterligere boosting og effektivisering av algeproduksjonen lf. Furthermore, further features are shown in fig. 4a,4b,5a,5b,6,7a,7b and 8a,8b where the gins 45,48 can be connected with a pipe or framework 99, where artificial light is attached, e.g. in the form of a rod or pipe light 98 which can be suspended in the framework 99 at appropriate distances from each other and which can then be rotated with the mixing gins 45 and ensure further boosting and streamlining of algae production lf.

Det er også vist et antall propellerpumper eller mixere 82 som kan være montert i grindene 45, som ytterligere kan sørge for en strømning i reaktoren 1 og som kan øke effektiviteten i algeproduksjonen. There is also shown a number of propeller pumps or mixers 82 which can be mounted in the gates 45, which can further ensure a flow in the reactor 1 and which can increase the efficiency of algae production.

Dette kan da skje i tillegg til at de nevnte forskjellige midlene 11,12,13 og81 blir renset og dosert i et hensiktsmessig blandingsforhold og at kunstif lys da vil kunne monters i bunn 47a og på vegger 47b i tillegg til luft som kan injiesers i bunn47a og i vegger 47b på en kontrollert måte og totalt sett da utgjøre en optimalisert prosess som er selvrensende og som både kan produsere, høste, avvanne og prosessere algebiomassen lf til flere ønskede produkter innenfor forbransen, kosmetikkbransjen, 'farmasøytisk industri og som ogsåkan tjene som buffer for oppdrettsanleggen ved en egen oksygenproduksjon og ved at avfall fra oppdrettsanlegg kan benyttes i sin heleht i reaktoren 1 algeproduksjon. This can then happen in addition to the aforementioned different agents 11,12,13 and 81 being cleaned and dosed in an appropriate mixing ratio and artificial light will then be able to be installed in the bottom 47a and on the walls 47b in addition to air that can be injected into the bottom 47a and in walls 47b in a controlled manner and overall then constitute an optimized process which is self-cleaning and which can both produce, harvest, dewater and process the algal biomass lf into several desired products within the fuel industry, the cosmetics industry, the pharmaceutical industry and which can also serve as a buffer for the breeding facility by a separate oxygen production and by the fact that waste from breeding facilities can be used in its entirety in reactor 1 algae production.

Dette gir en resirkelert miljøvennlig og effektiv utnyttelse av alle resurser i havområde uten at innsatsfaktorehne medfører noe vesentlige kostnader. This provides a recycled, environmentally friendly and efficient utilization of all resources in the sea area without the input factor leading to any significant costs.

Totalt sett vil dette kunne gjøre oppdrettsnæringen også mer effektiv og være et alternativ til fiskeolje i forproduksjonen, noe som igjen gir muligheter for vekst i oppdrettsnæringen. Overall, this will also make the farming industry more efficient and be an alternative to fish oil in pre-production, which in turn provides opportunities for growth in the farming industry.

Claims (1)

Patentkrav 1. Anordning for produksjon, innhøsting og avvanning av mikroalger lf der C02 blir tilførsel med vann og midler som skal til for en fotosyntese i og en spalting av algeceller til en øket biomassekarakterisert vedat en reaktor 1 har en eller flere bevegelige blande 45 og innhøstingsgrinder 48 som roterer rundt en senterlagerpakke 62 og som kan styres individuelt i horsontalplanet og som kan vippes eller vris opp og ned omkring en bom eller alksling 35 i og like over reaktorbassenget 1 og som gjør det mulig produksjon og innhøsting alger på en kontrollert, flekibel og effektiv måte i en kontinuerlig prosess uten ndøvendigvis å tappe ned algebiomassen lf i bassenget 1. Patentkrav 2. Fotobioreaktor i flg. krav 1. Karakterisert ved at omtalte blande og innhøstingsgrinder kan beveges i 2 høydenivåer for at algeproduksjon og innhøsting kan skje på en kontinuuerlig og fleksibel måte. Patentkrav 3. Fotobioreaktor i flg. krav 1 Karakterisert ved at reaktoren 1 har en innhøstingsrenne 42 hellende utover og nedover fra senter og at rennea 42 er tilsluttet en bunn 47 som utgjør en oppover og nedoverbakke 92,93 og som dermed kan gjøre at renna får en svak helning som igjen gjør at algebiomassen le som blir høstet i renna 42, strømmer av egen tyngde utover og nedover mot et avløp tilsluttet en yterligere avvanningsprosess 38,86,91. Patentkrav 4. Fotobioreaktor i flg. krav 3. Kaakterisert ved at rennen 42 har en nedover og utoverettet hellende bunn som ender opp i et oppsamlingstank 36 tilsluttet midler38,86 for avvanning og pressing av algebiomassen til et ønsket sluttprodukt. Patentkrav 5. Bioreaktor i flg. krav 1 Karakterisert ved at grindene er fleksiibelt opphengt i en bom 35 opplagret i et lukket vannfylt lager 62 og der grinedene 45,48 slepes langs bunnen 47 etter bommen 35 ved at denne er opplagret i periferien og på reaktoren 1,2 dekk 16 og som dermed kan roteres på en kontrollert måte. Patentkrav 6. Bioreaktor i flg krav 1 Karakterisert ved at Reaktoren har en sentralt orientert kontrol og maskinrom 80a i nivå over reaktoren 1 lysgjennomtrengende hus 3. Patentkrav 7. Bioreaktor i flg. krav 1 Karakterisert ved at det lukkete hus 3 er forbundet med en vifte 9, en sugeledning 7 og en kompressorpakke 87,87a,87b for oppsamling og komprimering av oksygenavgass 8 og som f. eks. kan lagres i trykkflasker 35 på plattformen 2. Patentkrav 8. Bioreaktor i flg. krav 1 Karakterisert ved at lompressorhuset og/eller komperssoren 87 ,er omsluttet av sjøvannsledningen 4 gjennom en varmeveksler 4b for å kjøle ned oksygennen 87og oppvarming av sjøvannet 4 som er tilslutettet pumpen 6 og filteresystemet 10. Patentkrav 9. Bioreaktor i flg. krav 8 Karakterisert ved at grindene 45 er forbundet stivt eller flekisbelt innbyrdes via rør ,wire,tauverk eller kjetting 98 og som i tillegg til å stive av grindne 45,48 kan utgjøre et oppheng for kunstig lys 99 som kan henges loddrett ned i reaktoren 1.Patent claim 1. Device for the production, harvesting and dewatering of microalgae lf where C02 is supplied with water and means needed for a photosynthesis in and a splitting of algae cells into an increased biomass characterized by a reactor 1 having one or more movable mixers 45 and harvesting grates 48 which rotates around a central bearing package 62 and which can be controlled individually in the horizontal plane and which can be tilted or twisted up and down around a boom or alksling 35 in and just above the reactor basin 1 and which enables the production and harvesting of algae on a controlled, flexible and efficient way in a continuous process without necessarily draining the algal biomass lf in the pool 1. Patent claim 2. Photobioreactor in the following claim 1. Characterized in that the mentioned mixing and harvesting grates can be moved in 2 height levels so that algae production and harvesting can take place on a continuous and flexible way. Patent claim 3. Photobioreactor in the following claim 1 Characterized in that the reactor 1 has a harvesting chute 42 sloping outwards and downwards from the center and that the chute 42 is connected to a bottom 47 which forms an uphill and downhill slope 92,93 and which can thus cause the chute to get a slight slope which in turn means that the algae biomass that is harvested in the chute 42 flows under its own weight outwards and downwards towards a drain connected to a further dewatering process 38,86,91. Patent claim 4. Photobioreactor in the following claim 3. Characterized in that the chute 42 has a downward and outward sloping bottom which ends in a collection tank 36 connected to means 38,86 for dewatering and pressing the algal biomass into a desired end product. Patent claim 5. Bioreactor in following claim 1 Characterized in that the gates are flexibly suspended in a boom 35 stored in a closed water-filled warehouse 62 and where the gates 45,48 are towed along the bottom 47 after the boom 35 in that it is stored in the periphery and on the reactor 1.2 tire 16 and which can thus be rotated in a controlled manner. Patent claim 6. Bioreactor in the following claim 1 Characterized in that the reactor has a centrally oriented control and machine room 80a at a level above the reactor 1 light-transmitting housing 3. Patent claim 7. Bioreactor in the following claim 1 Characterized in that the closed housing 3 is connected to a fan 9, a suction line 7 and a compressor pack 87,87a,87b for collecting and compressing oxygen waste gas 8 and which, for example, can be stored in pressure bottles 35 on the platform 2. Patent claim 8. Bioreactor in following claim 1 Characterized in that the air compressor housing and/or the compressor 87 is enclosed by the seawater line 4 through a heat exchanger 4b to cool down the oxygen 87 and heat the seawater 4 which is sealed off the pump 6 and the filter system 10. Patent claim 9. Bioreactor in following claim 8 Characterized by the fact that the gates 45 are connected rigidly or flexibly to each other via pipes, wires, ropes or chains 98 and which, in addition to stiffening the gates 45, 48, can constitute a suspension for artificial light 99 which can be hung vertically into the reactor 1.
NO20140975A 2014-07-08 2014-08-08 Bioreactor and process for microalgae production NO20140975A1 (en)

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Application Number Priority Date Filing Date Title
EP15818508.2A EP3167043B1 (en) 2014-07-08 2015-07-08 Bioreactor for production and harvesting of microalgae
PCT/NO2015/050125 WO2016007016A1 (en) 2014-07-08 2015-07-08 Bioreactor for production and harvesting of microalgae
CN201580042578.6A CN107155333B (en) 2014-07-08 2015-07-08 Bioreactor for producing and harvesting microalgae
NO20150893A NO340051B1 (en) 2014-07-08 2015-07-08 Bioreactor for production and harvesting of microalgae
US15/324,420 US20170158995A1 (en) 2014-07-08 2015-07-08 Bioreactor for production and harvesting of microalgae
JP2017522310A JP6621817B2 (en) 2014-07-08 2015-07-08 Bioreactors for the production and harvesting of microalgae

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