TWI615467B - Microalgae harvest module and method of harvesting microalgae - Google Patents
Microalgae harvest module and method of harvesting microalgae Download PDFInfo
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Abstract
一種微藻的採收方法。於含微藻細胞的培養液中添加絮凝劑與磁性粒子,以形成懸浮於培養液中的微藻磁性絮凝物。將含微藻磁性絮凝物的培養液置於採收容器中。對採收容器的外壁施加一磁場,使得微藻磁性絮凝物被吸附於採收容器的內壁上而與培養液分離。在微藻磁性絮凝物被吸附於採收容器的內壁上的情況下,移除採收容器中的培養液。移除磁場,取得微藻磁性絮凝物。另外,亦提供一種微藻採收模組。 A method of harvesting microalgae. A flocculant and magnetic particles are added to the culture solution containing the microalgae cells to form microalgae magnetic flocs suspended in the culture solution. The culture solution containing the microalgae magnetic floes is placed in a harvesting container. A magnetic field is applied to the outer wall of the harvesting container so that the microalgae magnetic flocs are adsorbed on the inner wall of the harvesting container to be separated from the culture liquid. In the case where the microalgae magnetic flocs are adsorbed on the inner wall of the harvesting container, the culture liquid in the harvesting container is removed. The magnetic field is removed to obtain microalgal magnetic floes. In addition, a microalgae harvesting module is also provided.
Description
本發明是有關於一種採收模組與採收方法,且特別是有關於一種微藻採收模組與微藻的採收方法。 The invention relates to a harvesting module and a harvesting method, and in particular to a method for harvesting a microalgae harvesting module and microalgae.
近數十年間,全球對於微藻生物質應用於食品、飼料、生質柴油以及化學製品的需求逐漸上升,微藻生物質具有極大的潛力可取代現今許多農作生物質來源。然而,依美國ASP(Aquatic Species Program)計畫所作的分析,濃縮分離與乾燥脫水程序所需成本約佔微藻生質柴油生產總成本38%,國際微藻生物質組織(ABO)也曾指出,微藻細胞的收集至少佔全部生產成本的20~30%。也是說,迄今微藻生產仍受限於高成本經濟價值產物。 In recent decades, global demand for microalgal biomass for food, feed, biodiesel, and chemicals has increased, and microalgal biomass has great potential to replace many of today's agricultural biomass sources. However, according to the analysis of the American ASP (Aquatic Species Program) program, the cost of the concentrated separation and drying dehydration process accounts for 38% of the total cost of microalgae biodiesel production. The International Microalgae Biomass Organization (ABO) also pointed out The collection of microalgae cells accounts for at least 20~30% of the total production cost. It is also said that microalgae production has so far been limited by high cost economic value products.
一般來說,在養殖微藻後,微藻的利用通常包括採收、乾燥、破壁與產物萃取等程序,其中採收程序對於產物的產率具有重大影響。目前已發展出多種微藻採收技術,主要包括離心採收、過濾採收、浮除採收,以及混凝採收等技術。其中,離心採收是微藻採收最常見的方法之一,其優點在於採收微藻細胞的效 率高達95%以上,但缺點為離心機之硬體設備費用高及運轉之能耗也高。因此,離心採收通常用於需要較純淨且具有高利潤之微藻產品。相反地,過濾採收具有低能耗的優點,但因其僅適於收集具有特定尺寸以上的微藻細胞,故其採收效率不高,且主要用於採收團聚生長之微細藻類。 In general, after the cultivation of microalgae, the utilization of microalgae usually includes procedures such as harvesting, drying, wall breaking and product extraction, wherein the harvesting process has a significant impact on the yield of the product. At present, a variety of microalgae harvesting technologies have been developed, including technologies such as centrifugal harvesting, filtration and harvesting, floatation and harvesting, and coagulation and harvesting. Among them, centrifugal harvesting is one of the most common methods for microalgae harvesting, which has the advantage of harvesting microalgae cells. The rate is as high as 95% or more, but the disadvantage is that the hardware cost of the centrifuge is high and the energy consumption for operation is also high. Therefore, centrifugal harvesting is commonly used for microalgae products that require relatively pure and high margins. Conversely, filtration has the advantage of low energy consumption, but it is only suitable for collecting microalgae cells with a specific size or more, so its recovery efficiency is not high, and it is mainly used for harvesting agglomerated microalgae.
浮除採收是使用高壓製造出微氣泡(micro-bubble),藉由微氣泡的上升將大部分的微藻細胞帶至液面,再以水流對上層液面進行收集。浮除採收的採收效率約可達到70%,採收後之培養液可回收而持續用於微藻養殖。然而,由於採收藻體時需持續地以高壓釋出微氣泡,因此具有高能耗的缺點。根據改變微藻細胞之表面電荷的方法,混凝採收通常為加入絮凝劑慢速攪拌或直接通入電流,以使微藻細胞產生聚集現象。由於聚集之微藻細胞能快速沉降,藉由過濾或直接移除上層之水分,可使微藻的採收效率達到約70~95%,且具有能耗較低的優點。此外,若不採取再一次絮凝沉降的微藻,其回收的藻體含水量仍高。雖可利用過濾方式處理之,不過此會導致混凝採收具有額外的成本效應。 The floating harvesting uses a high pressure to produce micro-bubbles, and most of the microalgae cells are brought to the liquid surface by the rise of the microbubbles, and the upper liquid level is collected by the water flow. The harvesting efficiency of the harvesting harvest can reach about 70%, and the culture liquid after harvesting can be recycled and continuously used for microalgae cultivation. However, since the microbubbles are continuously released at a high pressure when the algae is harvested, there is a disadvantage of high energy consumption. According to the method of changing the surface charge of the microalgae cells, the coagulation recovery is usually a slow agitation by adding a flocculant or a direct current to cause aggregation of the microalgae cells. Since the accumulated microalgae cells can settle quickly, the harvesting efficiency of the microalgae can be increased by about 70 to 95% by filtering or directly removing the moisture of the upper layer, and the energy consumption is low. In addition, if the microalgae settled by flocculation are not taken again, the water content of the recovered algae is still high. Although it can be treated by filtration, this will result in additional cost effects for coagulation recovery.
也就是說,由於微藻細胞僅具有約3~30μm的微小體積,且在持續維持高度生長的微藻養殖中,難以將藻體的密度維持在很高的狀態,因此目前的微藻細胞採收方法面臨成本與採收效率難以兩全的難題。然而,提高採收效率是微藻養殖工業所欲開發的關鍵技術之一,故有必要發展低能耗、易於量產、高採集率的微藻採收系統,以符合產業化可行性的需求。 That is to say, since the microalgae cells have only a small volume of about 3 to 30 μm, and it is difficult to maintain the density of the algae in a high state in the cultivation of microalgae which continuously maintains a high degree of growth, the current microalgae cells are collected. The method of receiving is difficult to solve both cost and harvesting efficiency. However, improving harvesting efficiency is one of the key technologies to be developed by the microalgae breeding industry. Therefore, it is necessary to develop a microalgae harvesting system with low energy consumption, easy mass production and high collection rate to meet the requirements of industrial feasibility.
本發明提供一種微藻採收模組,能達到低耗能與高採收效率的目的。 The invention provides a microalgae harvesting module, which can achieve the purpose of low energy consumption and high harvesting efficiency.
本發明的微藻採收模組包括養殖單元以及採收單元。養殖單元包括培養槽,培養槽用以容置含微藻細胞的培養液,而在欲採收微藻細胞時,將絮凝劑以及磁性粒子加入培養槽中,其中微藻細胞、絮凝劑以及磁性粒子於培養槽中形成懸浮於培養液中的微藻磁性絮凝物。採收單元包括採收容器與磁場產生裝置。採收容器與培養槽耦接,用以容置含有微藻磁性絮凝物的培養液。磁場產生裝置對採收容器的外壁提供可移除的磁場,在磁場存在的狀態下,微藻磁性絮凝物被聚集於採收容器的內壁上而與培養液分離。 The microalgae harvesting module of the invention comprises a breeding unit and a harvesting unit. The culture unit comprises a culture tank for accommodating the culture liquid containing the microalgae cells, and when the microalgae cells are to be collected, the flocculant and the magnetic particles are added to the culture tank, wherein the microalgae cells, the flocculant and the magnetic body The particles form microalgae magnetic floes suspended in the culture solution in the culture tank. The harvesting unit includes a harvesting container and a magnetic field generating device. The harvesting container is coupled to the culture tank for accommodating the culture liquid containing the microalgae magnetic floc. The magnetic field generating device provides a removable magnetic field to the outer wall of the harvesting container, and in the presence of the magnetic field, the microalgal magnetic flocs are collected on the inner wall of the harvesting container to be separated from the culture liquid.
在本發明的一實施例中,上述的採收單元為可拆卸式採收單元,可拆卸地連接於養殖單元。 In an embodiment of the invention, the harvesting unit is a detachable harvesting unit detachably coupled to the breeding unit.
在本發明的一實施例中,上述的採收單元更包括採集器,在移除磁場後,用以收集留存於採收容器中的微藻磁性絮凝物。 In an embodiment of the invention, the harvesting unit further includes a collector for collecting microalgae magnetic floes retained in the harvesting container after the magnetic field is removed.
在本發明的一實施例中,上述的採收容器為中空管,以及採集器為具有推桿的活塞,活塞與中空管的內壁為滑動式配合。 In an embodiment of the invention, the harvesting container is a hollow tube, and the collector is a piston having a push rod, and the piston and the inner wall of the hollow tube are in a sliding fit.
在本發明的一實施例中,上述的磁場產生裝置為永久磁鐵或電磁鐵。 In an embodiment of the invention, the magnetic field generating device is a permanent magnet or an electromagnet.
在本發明的一實施例中,更包括第一輸液管,其中培養 槽具有輸出口,採收容器具有輸入口,培養槽的輸出口經由第一輸液管與採收容器的輸入口連接。 In an embodiment of the invention, the first infusion tube is further included, wherein the culture The trough has an output port, and the harvesting container has an input port, and the output port of the culture trough is connected to the input port of the harvesting container via the first infusion tube.
在本發明的一實施例中,更包括回收單元,與採收單元連接,回收單元包括培養液儲存槽,培養液儲存槽與採收容器連接,用以儲存來自於採收容器的培養液。 In an embodiment of the invention, the recycling unit is further connected to the harvesting unit, and the recovery unit comprises a culture liquid storage tank connected to the harvesting container for storing the culture liquid from the harvesting container.
在本發明的一實施例中,更包括幫浦,用以將培養液儲存槽中的培養液抽吸至培養槽中。 In an embodiment of the invention, a pump is further included for pumping the culture solution in the culture solution storage tank into the culture tank.
在本發明的一實施例中,上述的培養槽為光生物反應器(photobioreactor)。 In an embodiment of the invention, the culture tank is a photobioreactor.
在本發明的一實施例中,上述的培養槽的材料包括聚氯乙烯(polyvinylchloride,PVC)、聚乙烯(polyethylene,PE)、聚甲基丙烯酸甲酯(polymethylmethacrylate,PMMA)或玻璃。 In an embodiment of the invention, the material of the culture tank comprises polyvinyl chloride (PVC), polyethylene (PE), polymethylmethacrylate (PMMA) or glass.
在本發明的一實施例中,上述的養殖單元更包括曝氣調控裝置,與培養槽的底部耦接。 In an embodiment of the invention, the aquaculture unit further includes an aeration control device coupled to the bottom of the culture tank.
本發明的微藻的採收方法包括以下步驟。於含微藻細胞的培養液中添加絮凝劑與磁性粒子,以形成懸浮於培養液中的微藻磁性絮凝物。將含微藻磁性絮凝物的培養液置於採收容器中。對採收容器的外壁施加一磁場,使得微藻磁性絮凝物被吸附於採收容器的內壁上而與培養液分離。在微藻磁性絮凝物被吸附於採收容器的內壁上的情況下,移除採收容器中的培養液。移除磁場,取得微藻磁性絮凝物。 The method of harvesting the microalgae of the present invention comprises the following steps. A flocculant and magnetic particles are added to the culture solution containing the microalgae cells to form microalgae magnetic flocs suspended in the culture solution. The culture solution containing the microalgae magnetic floes is placed in a harvesting container. A magnetic field is applied to the outer wall of the harvesting container so that the microalgae magnetic flocs are adsorbed on the inner wall of the harvesting container to be separated from the culture liquid. In the case where the microalgae magnetic flocs are adsorbed on the inner wall of the harvesting container, the culture liquid in the harvesting container is removed. The magnetic field is removed to obtain microalgal magnetic floes.
在本發明的一實施例中,取得微藻磁性絮凝物的方法包 括使用一採集器聚集留存於採收容器中的微藻磁性絮凝物。 In an embodiment of the invention, a method for obtaining microalgae magnetic flocs A microalgae magnetic floc retained in the harvesting container is collected using a collector.
在本發明的一實施例中,上述的採收容器為中空管,以及採集器為具有推桿的活塞,活塞與中空管的內壁為滑動式配合。 In an embodiment of the invention, the harvesting container is a hollow tube, and the collector is a piston having a push rod, and the piston and the inner wall of the hollow tube are in a sliding fit.
在本發明的一實施例中,更包括回收自採收容器移除的培養液。 In an embodiment of the invention, the culture fluid removed from the harvesting container is further included.
在本發明的一實施例中,上述的絮凝劑為含金屬的無機凝聚劑或聚合物凝聚劑。 In an embodiment of the invention, the flocculating agent is a metal-containing inorganic coagulant or a polymer coagulant.
在本發明的一實施例中,上述的含金屬的無機凝聚劑包括三氯化鐵(FeCl3)或三氯化鋁(AlCl3)。 In an embodiment of the invention, the metal-containing inorganic coagulant comprises ferric chloride (FeCl 3 ) or aluminum trichloride (AlCl 3 ).
在本發明的一實施例中,上述的磁性粒子包括四氧化三鐵(Fe3O4)、三氧化二鐵(Fe2O3)或其組合。 In an embodiment of the invention, the magnetic particles include ferroferric oxide (Fe 3 O 4 ), ferric oxide (Fe 2 O 3 ), or a combination thereof.
基於上述,本發明之微藻採收模組與微藻的採收方法是使用絮凝劑與磁性粒子以及施加磁場,以採收具有緊密結構與低體積含水量的微藻磁性絮凝物。如此一來,可實現低能耗、高採收效率且具有水資源再利用的微藻採收,符合產業發展之需求。 Based on the above, the microalgae harvesting module and the microalgae of the present invention are harvested by using a flocculating agent and magnetic particles and applying a magnetic field to recover microalgal magnetic floes having a compact structure and a low volumetric water content. In this way, the microalgae harvesting with low energy consumption, high recovery efficiency and water reuse can be realized, which meets the needs of industrial development.
為讓本發明的上述特徵和優點能更明顯易懂,下文特舉實施例,並配合所附圖式作詳細說明如下。 The above described features and advantages of the invention will be apparent from the following description.
10‧‧‧微藻採收模組 10‧‧‧Microalgae harvesting module
100‧‧‧養殖單元 100‧‧‧ farming unit
110‧‧‧培養槽 110‧‧‧ culture tank
112、114、212、214、412、414‧‧‧輸液口 112, 114, 212, 214, 412, 414 ‧ ‧ infusion port
120‧‧‧曝氣調控裝置 120‧‧‧Aeration control device
200‧‧‧採收單元 200‧‧‧ harvesting unit
210‧‧‧採收容器 210‧‧‧ harvesting containers
210a‧‧‧外壁 210a‧‧‧ outer wall
210b‧‧‧內壁 210b‧‧‧ inner wall
220‧‧‧磁場產生裝置 220‧‧‧Magnetic field generating device
230‧‧‧採集器 230‧‧‧ Collector
232‧‧‧推桿 232‧‧‧Put
234‧‧‧活塞 234‧‧‧Piston
300‧‧‧幫浦 300‧‧‧ pump
400‧‧‧回收單元 400‧‧‧Recycling unit
410‧‧‧培養液儲存槽 410‧‧‧ culture solution storage tank
510、520、530‧‧‧輸液管 510, 520, 530‧‧‧ Infusion tube
F‧‧‧微藻磁性絮凝物 F‧‧‧Microalgae magnetic flocs
MD、MD’‧‧‧培養液 MD, MD’‧‧‧ culture solution
MF‧‧‧磁場 MF‧‧‧ magnetic field
S10~S50‧‧‧步驟 S10~S50‧‧‧Steps
圖1是依照本發明一實施例的微藻採收模組的示意圖。 1 is a schematic view of a microalgae harvesting module in accordance with an embodiment of the present invention.
圖2A至圖2C為圖1的採收單元的局部放大示意圖。 2A to 2C are partial enlarged views of the harvesting unit of Fig. 1.
圖3A與圖3B為本發明一實施例的微藻採收模組的採收單元的局部示意圖。 3A and 3B are partial schematic views of a harvesting unit of a microalgae harvesting module according to an embodiment of the invention.
圖4是依照本發明一實施例的微藻的採收方法的流程示意圖。 4 is a schematic flow chart of a method for harvesting microalgae according to an embodiment of the present invention.
圖5A為實驗例1中的對照組的顯微照片,其中培養液中僅含微藻細胞。 Fig. 5A is a photomicrograph of a control group in Experimental Example 1, in which the culture solution contains only microalgae cells.
圖5B為實驗例1中的實驗組的顯微照片,其中培養液中含微藻細胞、絮凝劑及磁性粒子。 Fig. 5B is a photomicrograph of the experimental group in Experimental Example 1, in which the culture solution contains microalgae cells, a flocculating agent, and magnetic particles.
圖6為實驗例2中添加不同濃度的Fe3O4磁性粒子的微藻細胞的採收效率折線圖。 Fig. 6 is a line graph showing the recovery efficiency of microalgae cells to which different concentrations of Fe 3 O 4 magnetic particles were added in Experimental Example 2.
圖7為實驗例3中連續進行14天的培養與兩次微藻回收後,微藻培養液重複使用於微藻細胞培養的生長折線圖。 Fig. 7 is a growth line graph of the microalgae culture solution repeatedly used in microalgae cell culture after the continuous culture for 14 days and the recovery of the microalgae in Experimental Example 3.
圖1是依照本發明一實施例的微藻採收模組的示意圖。請參照圖1,微藻採收模組10包括養殖單元100以及採收單元200。在本實施例中,微藻採收模組10例如是更包括幫浦300與回收單元400。 1 is a schematic view of a microalgae harvesting module in accordance with an embodiment of the present invention. Referring to FIG. 1 , the microalgae recovery module 10 includes a culture unit 100 and a recovery unit 200 . In the present embodiment, the microalgae recovery module 10 includes, for example, a pump 300 and a recovery unit 400.
養殖單元100包括培養槽110,培養槽110用以容置含微藻細胞的培養液MD、絮凝劑(未繪示)以及磁性粒子(未繪示),其中微藻細胞、絮凝劑以及磁性粒子於培養槽110中形成懸浮於培養液MD中的微藻磁性絮凝物F。詳細地說,先在培養槽110中以 培養液MD培養微藻細胞,在微藻細胞培養完成後(即培養末期時),才將絮凝劑以及磁性粒子加入培養槽110中,使得微藻細胞、絮凝劑以及磁性粒子形成微藻磁性絮凝物F。在本實施例中,養殖單元100例如是包括由多個培養槽110並聯而成的陣列,但並不用以限制本發明。在其他實施例中,培養槽110亦可能為其他排列方式,例如以串聯或者串聯與並聯之結合的方式排列。此外,培養槽110的數目例如分別是1個~100個,並無特別限定,可視需求而進行調整。但並不用以限制本發明。其中,培養槽110例如是密閉式光生物反應器或開放式培養池等,培養槽110例如是管狀容器。養殖單元100例如是更包括曝氣調控裝置120,與培養槽110的底部耦接。培養槽110的光照來源例如是太陽光或人造光源如日光燈、發光二極體等。培養槽的材料包括聚氯乙烯、聚乙烯、聚甲基丙烯酸甲酯、玻璃或其他可透光材料。在本實施例中 The culture unit 100 includes a culture tank 110 for accommodating the culture liquid MD containing microalgae cells, a flocculating agent (not shown), and magnetic particles (not shown), wherein the microalgae cells, the flocculating agent and the magnetic particles The microalgae magnetic floc F suspended in the culture solution MD is formed in the culture tank 110. In detail, first in the culture tank 110 The culture medium MD cultures the microalgae cells, and after the microalgae cell culture is completed (ie, at the end of the culture), the flocculant and the magnetic particles are added to the culture tank 110, so that the microalgae cells, the flocculating agent and the magnetic particles form microalgae magnetic flocculation. Matter F. In the present embodiment, the culture unit 100 includes, for example, an array in which a plurality of culture tanks 110 are connected in parallel, but is not intended to limit the present invention. In other embodiments, the culture tanks 110 may also be arranged in other ways, such as in series or in a combination of series and parallel. Further, the number of the culture tanks 110 is, for example, one to 100, and is not particularly limited, and may be adjusted as needed. However, it is not intended to limit the invention. The culture tank 110 is, for example, a closed photobioreactor or an open culture tank, and the culture tank 110 is, for example, a tubular container. The culture unit 100 further includes, for example, an aeration control device 120 coupled to the bottom of the culture tank 110. The illumination source of the culture tank 110 is, for example, sunlight or an artificial light source such as a fluorescent lamp, a light-emitting diode, or the like. The material of the culture tank includes polyvinyl chloride, polyethylene, polymethyl methacrylate, glass or other permeable material. In this embodiment
上述微藻株之品系例如是小球藻屬(Chlorella)、綠藻、藍綠藻、擬球藻屬(Nannochloropsis)、螺旋藻屬(Spirulina)等鞭金藻屬(Isochrysis)、聚球藻屬(Synechococcus)或紅球藻屬(Haematococcus)。較佳之微藻株例如是綠藻、藍綠藻、擬球藻等鞭金藻或紅球藻。 The above-described microalgae strains, for example strains of the genus Chlorella (Chlorella), green algae, blue-green algae Nannochloropsis sp (Nannochloropsis), Spirulina (fromSpirulina) Isochrysis sp (Isochrysis), Synechococcus ( Synechococcus ) or Haematococcus . Preferred microalgae strains are, for example, green algae, blue-green algae, Chlorella vulgaris, or Haematococcus.
絮凝劑例如是含金屬的無機凝聚劑或聚合物凝聚劑。在本實施例中,絮凝劑例如是三氯化鐵等可溶於液體中成Fe3+、Fe2+之無機金屬溶液或三氯化鋁。磁性粒子例如是包含能夠被磁場吸 引之粒子,包括四氧化三鐵、三氧化二鐵或其組合。在本實施例中,磁性粒子的濃度例如是12.5mg/L至50mg/L。 The flocculating agent is, for example, a metal-containing inorganic coagulant or a polymer coagulant. In the present embodiment, the flocculating agent is, for example, an inorganic metal solution such as ferric chloride which is soluble in a liquid to form Fe 3+ or Fe 2+ or aluminum trichloride. The magnetic particles are, for example, particles comprising a magnetic field attracting, including triiron tetroxide, ferric oxide or a combination thereof. In the present embodiment, the concentration of the magnetic particles is, for example, 12.5 mg/L to 50 mg/L.
在本實施例中,培養槽110具有輸液口112與輸液口114,輸液口112例如是培養槽110的液體輸入口,以及輸液口114例如是培養槽110的液體輸出口。其中,輸液口112與輸液口114處例如是更設置有調節閥(未繪示),分別用以控制流入培養槽110的含微藻細胞的培養液的流速,以及流出培養槽110的含微藻磁性絮凝物F的培養液的流速。 In the present embodiment, the culture tank 110 has an infusion port 112 and an infusion port 114. The infusion port 112 is, for example, a liquid inlet port of the culture tank 110, and the infusion port 114 is, for example, a liquid outlet port of the culture tank 110. The infusion port 112 and the infusion port 114 are, for example, further provided with a regulating valve (not shown) for controlling the flow rate of the culture medium containing the microalgae cells flowing into the culture tank 110, and the microflow flowing out of the culture tank 110. The flow rate of the culture solution of the algal magnetic floc F.
採收單元200包括採收容器210與磁場產生裝置220。採收容器210與培養槽110耦接,用以容置含有微藻磁性絮凝物F的培養液MD。在本實施例中,採收單元200例如是可拆卸式採收單元,可拆卸地連接於養殖單元100。也就是說,可以將採收單元200與養殖單元100分離,以方便進行後續處理。在本實施例中,採收容器210例如是管狀容器,具有輸液口212與輸液口214。輸液口212例如是採收容器210的液體輸入口,以及輸液口214例如是採收容器210的液體輸出口。在本實施例中,微藻採收模組10更包括第一輸液管510,連接培養槽110的輸液口114與採收容器210的輸液口212。也就是說,經由第一輸液管510,含有微藻磁性絮凝物F的培養液MD由培養槽110進入採收容器210。 The harvesting unit 200 includes a recovery container 210 and a magnetic field generating device 220. The harvesting container 210 is coupled to the culture tank 110 for accommodating the culture liquid MD containing the microalgae magnetic floc F. In the present embodiment, the harvesting unit 200 is, for example, a detachable harvesting unit that is detachably coupled to the culture unit 100. That is, the harvesting unit 200 can be separated from the farming unit 100 to facilitate subsequent processing. In the present embodiment, the harvesting container 210 is, for example, a tubular container having an infusion port 212 and an infusion port 214. The infusion port 212 is, for example, a liquid inlet port of the collection container 210, and the infusion port 214 is, for example, a liquid outlet port of the collection container 210. In the present embodiment, the microalgae recovery module 10 further includes a first infusion tube 510 that connects the infusion port 114 of the culture tank 110 with the infusion port 212 of the recovery container 210. That is, the culture liquid MD containing the microalgae magnetic floc F enters the recovery container 210 through the culture tank 110 via the first infusion tube 510.
圖2A至圖2C為圖1的採收單元200的局部放大示意圖。磁場產生裝置220對採收容器210的外壁210a提供可移除的磁場MF。詳細地說,如圖2A所示,在提供磁場MF之前,含有微藻 磁性絮凝物F的培養液MD留存於採收容器210中。在提供磁場MF的狀態下,如圖2B所示,微藻磁性絮凝物F被聚集於採收容器的內壁210b上而與培養液MD’分離。當磁場MF提供於採收容器的外壁210a時,微藻磁性絮凝物F會被吸附於採收容器的內壁210b上而與培養液MD分離,故培養液MD’例如是澄清的培養液。在移除培養液MD’以及移除磁場MF後,如圖2C所示,微藻磁性絮凝物F留存於採收容器210中。特別說明的是,在本實施例中,由於微藻磁性絮凝物F呈藻泥狀,因此如圖2C所示,在移除磁場MF後,微藻磁性絮凝物F實質上仍會黏附於採收容器的內壁210b上。 2A to 2C are partial enlarged views of the harvesting unit 200 of Fig. 1. The magnetic field generating device 220 provides a removable magnetic field MF to the outer wall 210a of the recovery container 210. In detail, as shown in FIG. 2A, the microalgae are contained before the magnetic field MF is supplied. The culture solution MD of the magnetic floc F remains in the recovery container 210. In the state where the magnetic field MF is supplied, as shown in Fig. 2B, the microalgae magnetic floc F is collected on the inner wall 210b of the harvesting container to be separated from the culture liquid MD'. When the magnetic field MF is supplied to the outer wall 210a of the harvesting container, the microalgae magnetic floc F is adsorbed on the inner wall 210b of the collecting container to be separated from the culture liquid MD, so that the culture liquid MD' is, for example, a clarified culture liquid. After the culture solution MD' is removed and the magnetic field MF is removed, as shown in FIG. 2C, the microalgae magnetic floc F remains in the harvesting container 210. In particular, in the present embodiment, since the microalgae magnetic floc F is in the form of algal mud, as shown in FIG. 2C, after the magnetic field MF is removed, the microalgae magnetic floc F remains substantially adhered to the mining. The inner wall 210b of the container is closed.
磁場產生裝置220例如是永久磁鐵或電磁鐵,其中電磁鐵以通電流來產生磁場。磁場產生裝置220例如是配置於採收容器210的外壁210a的相對兩側,以形成諸如圖2B所示的磁場MF。在圖1中,是以一組平行設置的磁場產生裝置220為例,但在其他實施例中,也可以設置多組平行磁場產生裝置。 The magnetic field generating device 220 is, for example, a permanent magnet or an electromagnet in which an electromagnet generates a magnetic field by a current. The magnetic field generating device 220 is disposed, for example, on opposite sides of the outer wall 210a of the harvesting container 210 to form a magnetic field MF such as that shown in FIG. 2B. In Fig. 1, a set of magnetic field generating devices 220 arranged in parallel is taken as an example, but in other embodiments, a plurality of sets of parallel magnetic field generating devices may be provided.
如圖3A與圖3B所示,在本實施例中,採收單元200例如是更包括採集器230,當將採收單元200由微藻採收模組10中卸除時,可使用採集器230來收集留存於採收容器210中的微藻磁性絮凝物F。在本實施例中,採收容器210例如是中空管,採集器230例如是具有推桿232的活塞234,活塞234與中空管的內壁為滑動式配合。當然,本發明不以此為限,在其他實施例中,採收容器210與採集器230也可以具有其他結構。 As shown in FIG. 3A and FIG. 3B, in the embodiment, the harvesting unit 200 further includes a collector 230. When the harvesting unit 200 is removed from the microalgae recovery module 10, the collector can be used. 230 collects the microalgae magnetic floc F remaining in the harvesting container 210. In the present embodiment, the harvesting container 210 is, for example, a hollow tube, and the collector 230 is, for example, a piston 234 having a push rod 232 that is in sliding engagement with the inner wall of the hollow tube. Of course, the present invention is not limited thereto. In other embodiments, the recovery container 210 and the collector 230 may have other structures.
在本實施例中,如圖1所示,回收單元400與採收單元200連接。回收單元400例如是包括培養液儲存槽410,培養液儲存槽410與採收容器210連接,用以儲存來自於採收容器210的培養液MD’。培養液儲存槽410具有輸液口412與輸液口414,輸液口412例如是培養液儲存槽410的液體輸入口,以及輸液口414例如是培養液儲存槽410的液體輸出口。在本實施例中,微藻採收模組10更包括第二輸液管520,連接採收容器210的輸液口214與培養液儲存槽410的輸液口412。也就是說,經由第二輸液管520,與微藻磁性絮凝物F分離的培養液MD’由採收容器210進入培養液儲存槽410。此外,在本實施例中,微藻採收模組10更包括第三輸液管530,連接培養液儲存槽410的輸液口414與培養槽110的輸液口112。也就是說,經由第三輸液管530,回收的培養液MD’由培養液儲存槽410進入培養槽110。在本實施例中,幫浦300例如是與回收單元400連接,用以將培養液儲存槽410中的培養液MD’抽吸至培養槽110中。如此一來,能夠達到再利用培養液MD’的目的。 In the present embodiment, as shown in FIG. 1, the recovery unit 400 is connected to the recovery unit 200. The recovery unit 400 includes, for example, a culture solution storage tank 410 connected to the recovery container 210 for storing the culture solution MD' from the recovery container 210. The culture solution storage tank 410 has an infusion port 412 and an infusion port 414. The infusion port 412 is, for example, a liquid inlet port of the culture solution storage tank 410, and the infusion port 414 is, for example, a liquid outlet port of the culture solution storage tank 410. In the present embodiment, the microalgae recovery module 10 further includes a second infusion tube 520 that connects the infusion port 214 of the recovery container 210 with the infusion port 412 of the culture solution storage tank 410. That is, the culture liquid MD' separated from the microalgae magnetic floc F via the second infusion tube 520 enters the culture solution storage tank 410 from the recovery container 210. In addition, in the embodiment, the microalgae recovery module 10 further includes a third infusion tube 530 connected to the infusion port 414 of the culture solution storage tank 410 and the infusion port 112 of the culture tank 110. That is, the recovered culture solution MD' is introduced into the culture tank 110 from the culture solution storage tank 410 via the third infusion tube 530. In the present embodiment, the pump 300 is connected, for example, to the recovery unit 400 for sucking the culture solution MD' in the culture solution storage tank 410 into the culture tank 110. In this way, the purpose of reusing the culture solution MD' can be achieved.
在本實施例中,回收單元400例如是更包括一濁度計(未繪示),用以量測回收的培養液MD’的濁度,以偵測培養液MD’中的生物質濃度。再者,由於採收單元200在密閉式或開放式環境下皆可運作,因此微藻採收模組10可以是密閉式或開放式系統。 In the present embodiment, the recovery unit 400 further includes, for example, a turbidity meter (not shown) for measuring the turbidity of the recovered culture solution MD' to detect the biomass concentration in the culture solution MD'. Moreover, since the harvesting unit 200 can operate in a closed or open environment, the microalgae harvesting module 10 can be a closed or open system.
接下來將以上述的微藻採收模組10為例來說明本發明的一實施例的微藻的採收方法,但本發明不以此為限。也就是說, 可以藉由其他設備來實施本發明的微藻的採收方法。 Next, the above-described microalgae recovery module 10 will be described as an example to describe the method of harvesting microalgae according to an embodiment of the present invention, but the present invention is not limited thereto. That is, The method of harvesting the microalgae of the present invention can be carried out by other equipment.
圖4是依照本發明一實施例的微藻的採收方法的流程示意圖。請同時參照圖1至圖4,首先,進行步驟S10,於含微藻細胞的培養液MD中添加絮凝劑與磁性粒子,以形成懸浮於培養液MD中的微藻磁性絮凝物F。在本實施例中,此步驟S10包括將含微藻細胞的培養液MD置於培養槽110中,培養微藻細胞,在微藻細胞培養完成後(及培養末期時),才將絮凝劑以及磁性粒子加入培養槽110中,使得微藻細胞、絮凝劑以及磁性粒子形成微藻磁性絮凝物F。其中,絮凝劑會改變培養液MD中微藻細胞的表面電荷,在此過程中,微藻細胞會與磁性粒子形成具有磁性的微藻磁性絮凝物F。 4 is a schematic flow chart of a method for harvesting microalgae according to an embodiment of the present invention. Referring to FIG. 1 to FIG. 4 simultaneously, first, step S10 is performed to add a flocculating agent and magnetic particles to the culture liquid MD containing microalgae cells to form microalgae magnetic floc F suspended in the culture liquid MD. In this embodiment, the step S10 includes placing the culture medium MD containing the microalgae cells in the culture tank 110, culturing the microalgae cells, and after the microalgae cell culture is completed (and at the end of the culture), the flocculant and the flocculant are The magnetic particles are added to the culture tank 110 such that the microalgae cells, the flocculating agent, and the magnetic particles form the microalgae magnetic floc F. Among them, the flocculant changes the surface charge of the microalgae cells in the culture medium MD, and in the process, the microalgae cells form a magnetic microalgae magnetic floc F with the magnetic particles.
接著,進行步驟S20,將含微藻磁性絮凝物F的培養液MD置於採收容器210中。在本實施例中,例如是打開控制輸液口112的調節閥並藉由調節閥控制流速,使得含微藻磁性絮凝物F的培養液MD經由第一輸液管510流向採收容器210,如圖2A所示。 Next, in step S20, the culture solution MD containing the microalgae magnetic floc F is placed in the harvesting container 210. In the present embodiment, for example, the regulating valve for controlling the infusion port 112 is opened and the flow rate is controlled by the regulating valve, so that the culture liquid MD containing the microalgae magnetic floc F flows to the harvesting container 210 via the first infusion tube 510, as shown in the figure. 2A is shown.
然後,如圖2B所示,進行步驟S30,對採收容器210的外壁210a施加磁場MF,使得微藻磁性絮凝物F被吸附於採收容器210的內壁210b上而與培養液MD’分離。在本實施例中,此步驟S30包括開啟產生磁場MF的裝置或者是將磁場產生裝置放置於採收容器210的外壁210a上。如此一來,帶有磁性粒子的微藻磁性絮凝物F在通過採收容器210時,會被採收容器210外的磁 場吸引,進而附著在採收容器210的內壁210b上。此時,採收容器210中的培養液MD’例如是實質上除去微藻磁性絮凝物F的培養液MD’。 Then, as shown in FIG. 2B, step S30 is performed to apply a magnetic field MF to the outer wall 210a of the harvesting container 210 so that the microalgae magnetic floc F is adsorbed on the inner wall 210b of the harvesting container 210 to be separated from the culture liquid MD'. . In the present embodiment, this step S30 includes turning on the means for generating the magnetic field MF or placing the magnetic field generating means on the outer wall 210a of the harvesting container 210. As a result, the microalgae magnetic floc F with magnetic particles is collected by the magnetic material outside the container 210 when passing through the recovery container 210. The field is attracted and attached to the inner wall 210b of the harvesting container 210. At this time, the culture liquid MD' in the recovery container 210 is, for example, a culture liquid MD' which substantially removes the microalgae magnetic floc F.
然後,如圖2C所示,進行步驟S40,在微藻磁性絮凝物F被吸附於採收容器210的內壁210b上的情況下,移除採收容器210中的培養液MD’。在本實施例中,此步驟S40更包括回收自採收容器210移除的培養液MD’。‘進行步驟S50,移除磁場MF,取得微藻磁性絮凝物F。在本實施例中,如圖3A與圖3B所示,此步驟S50包括由微藻採收模組10中拆卸採收容器210,接著移除磁場MF,其中微藻磁性絮凝物F實質上留存於採收容器210的內壁210b上。然後,藉由推動推桿232使活塞234於採收容器210中移動,進而將微藻磁性絮凝物F由採收容器210中向外推出,再收集微藻磁性絮凝物F。如此一來,完成微藻磁性絮凝物F的採收。 Then, as shown in Fig. 2C, step S40 is performed to remove the culture liquid MD' in the recovery container 210 in the case where the microalgae magnetic floc F is adsorbed on the inner wall 210b of the recovery container 210. In the present embodiment, this step S40 further includes recovering the culture liquid MD' removed from the recovery container 210. 'Step S50 is performed to remove the magnetic field MF to obtain the microalgae magnetic floc F. In this embodiment, as shown in FIG. 3A and FIG. 3B, the step S50 includes disassembling the recovery container 210 from the microalgae recovery module 10, and then removing the magnetic field MF, wherein the microalgae magnetic floc F is substantially retained. On the inner wall 210b of the recovery container 210. Then, by pushing the push rod 232 to move the piston 234 in the recovery container 210, the microalgae magnetic floc F is pushed out from the recovery container 210, and the microalgae magnetic floc F is collected. In this way, the harvesting of the microalgal magnetic floc F is completed.
在本實施例中,更包括利用培養液儲存槽410中的培養液MD’進行另一次的微藻採收。詳細地說,首先,使用濁度計偵測培養液儲存槽410中培養液MD’中的殘餘的生物質濃度。接著,根據所偵測出的生物質濃度,於培養液MD’中添加培養微藻所需要的營養液。然後,使培養液MD’經由第三輸液管530回流至培養槽110中以進行用於微藻採收的另一次培養。特別一提的是,本實施例之微藻的採收方法不會影響後續之油脂萃取效率。 In the present embodiment, the microalgae harvesting is further performed by using the culture solution MD' in the culture solution storage tank 410. In detail, first, the residual biomass concentration in the culture solution MD' in the culture solution storage tank 410 is detected using a turbidimeter. Next, the nutrient solution required for culturing the microalgae is added to the culture solution MD' based on the detected biomass concentration. Then, the culture solution MD' is returned to the culture tank 110 via the third infusion tube 530 to perform another culture for microalgae harvesting. In particular, the method of harvesting the microalgae of the present embodiment does not affect the subsequent oil extraction efficiency.
在上述之微藻採收模組與微藻的採收方法中,藉由絮凝 劑使得微藻細胞與磁性粒子形成具有磁性的微藻磁性絮凝物,因此可藉由施加磁場來採收微藻磁性絮凝物。特別是,由於微藻磁性絮凝物會被吸附於採收容器的內壁上,因此可以輕易地與採收容器內的培養液分離,進而得到具有緊密結構與低的體積含水量的微藻磁性絮凝物。此外,由於微藻磁性絮凝物與培養液具有良好的分離效果,因此可以回收培養液以重複利用。如此一來,可實現低能耗、低成本、高採收效率且具有水資源再利用的微藻採收,符合產業發展之需求。 In the above-mentioned microalgae harvesting module and microalgae harvesting method, by flocculation The agent causes the microalgae cells to form magnetic microalgae magnetic flocs with the magnetic particles, so that the microalgae magnetic flocs can be harvested by applying a magnetic field. In particular, since the microalgae magnetic flocs are adsorbed on the inner wall of the harvesting container, they can be easily separated from the culture liquid in the harvesting container, thereby obtaining microalgae magnetic properties having a compact structure and a low volumetric water content. Flocs. In addition, since the microalgae magnetic flocs have a good separation effect from the culture solution, the culture solution can be recovered for reuse. In this way, microalgae harvesting with low energy consumption, low cost, high harvesting efficiency and water reuse can be realized, which meets the needs of industrial development.
接下來將以實驗例來說明本發明之微藻的採收方法的採收效率。 Next, the recovery efficiency of the harvesting method of the microalgae of the present invention will be described by way of an experimental example.
實驗例1:微藻磁性絮凝物的形成Experimental Example 1: Formation of microalgae magnetic flocs
於此實驗例中,提供含微藻的培養液,微藻為小球藻(Chlorella sp.),培養液為人工海水,經養殖之藻株濃度約為2公克微藻/公升培養液。將上述含微藻的培養液分為實驗組與對照組,並於實驗組中進一步添加濃度為10mL/L培養液的三氯化鐵作為無機金屬絮凝劑與濃度為25mg/L的四氧化三鐵作為磁性粒子。使用光學顯微鏡觀察對照組與實驗組,結果分別如圖5A與圖5B所示。 In this experimental example, a culture solution containing microalgae is provided, the microalgae is Chlorella sp., the culture solution is artificial seawater, and the cultured algae strain has a concentration of about 2 g of microalgae per liter of culture liquid. The above microalgae-containing culture solution was divided into an experimental group and a control group, and further added with a concentration of 10 mL/L of the culture solution of ferric chloride as an inorganic metal flocculant and a concentration of 25 mg/L of tetraoxide three in the experimental group. Iron acts as a magnetic particle. The control group and the experimental group were observed using an optical microscope, and the results are shown in Fig. 5A and Fig. 5B, respectively.
由圖5A與圖5B可知,比較例的微藻會散佈在培養液中,而實驗例的微藻會與磁性粒子聚集成微藻磁性絮凝物。也就是說,微藻與磁性粒子會在絮凝劑的存在下形成微藻磁性絮凝物。 5A and 5B, the microalgae of the comparative example was dispersed in the culture solution, and the microalgae of the experimental example was aggregated with the magnetic particles to integrate the microalgae magnetic flocs. That is, the microalgae and magnetic particles form microalgal magnetic floes in the presence of a flocculant.
實驗例2:微藻的採收效率Experimental Example 2: Harvesting efficiency of microalgae
使用上述實施例的微藻採收模組來進行微藻的採收。於此實驗例中,經養殖之微藻細胞濃度約為0.6公克微藻/公升培養液,分別於上述含微藻的培養液中添加濃度為12.5mg/L、25mg/L、37.5mg/L以及50mg/L培養液的四氧化三鐵磁性粒子。實驗過程中,在將含微藻磁性絮凝物的培養液導入採收容器後,對採收容器施加持續不同時間的磁場,而後測量培養液儲存槽所回收的培養液中的微藻細胞濃度,其中磁場的表面磁通密度為4700~4900高斯(吸引力為77.8牛頓)。根據導入採收容器前的微藻細胞濃度與培養液儲存槽所回收的微藻細胞濃度,計算出微藻細胞的採收效率,其採收效率折線圖如圖6所示。 The microalgae harvesting module of the above embodiment was used to carry out the harvesting of the microalgae. In this experimental example, the cultured microalgae cells have a concentration of about 0.6 g of microalgae/liter of culture medium, and the concentrations of the microalgae-containing medium are respectively added to the culture medium containing 12.5 mg/L, 25 mg/L, and 37.5 mg/L. And ferroferric oxide magnetic particles of 50 mg/L of the culture solution. During the experiment, after the culture liquid containing the microalgae magnetic flocs is introduced into the harvesting container, the magnetic field of the harvesting container is applied for different time periods, and then the concentration of the microalgae cells in the culture liquid recovered by the culture liquid storage tank is measured. The surface magnetic flux density of the magnetic field is 4700~4900 Gauss (attractiveness is 77.8 Newtons). According to the microalgae cell concentration before the introduction of the harvesting container and the concentration of the microalgae cells recovered in the culture solution storage tank, the harvesting efficiency of the microalgae cells was calculated, and the recovery efficiency line diagram is shown in FIG. 6 .
由圖6中的採收效率折線圖,可知當添加濃度為12.5mg/L、25mg/L、37.5mg/L以及50mg/L培養液的四氧化三鐵磁性粒子時,微藻細胞的採收效率於磁場持續30秒後就有顯著效果,且微藻細胞的採收效率磁場持續60秒後就能達到90%以上的採收效率。此外,所形成的微藻磁性絮凝物單位體積水含量低,採收濃度可高達150g/L。以此實驗例所得數值估算,一公噸的微藻液只需要添加約20公克的磁性粒子就可以採收微藻細胞。 From the recovery efficiency line graph in Fig. 6, it can be seen that when the ferroferric oxide magnetic particles are added at a concentration of 12.5 mg/L, 25 mg/L, 37.5 mg/L, and 50 mg/L, the microalgae cells are harvested. The efficiency has a significant effect after the magnetic field lasts for 30 seconds, and the recovery efficiency of the microalgae cells can reach more than 90% of the harvesting efficiency after 60 seconds. In addition, the microalgae magnetic floc formed has a low water content per unit volume and a harvesting concentration of up to 150 g/L. Based on the values obtained in this experimental example, one metric ton of microalgae solution can be harvested by adding only about 20 grams of magnetic particles.
實驗例3:培養液的回收利用Experimental Example 3: Recycling of culture solution
使用上述實施例的微藻採收模組來進行微藻的採收。於此實驗例中,依序進行三次培養。實驗進行過程中,維持相同的環境溫度、培養液溫度、培養液pH值及光照等環境條件,並依據682nm波長下的吸光值(OD)來檢測微藻的生長情形。首先,於 養殖單元中加入含微藻細胞的培養液(稱為第一次培養液)進行第一次培養,養殖4天後,微藻細胞濃度由0.2g/L生長至1.25g/L,將此含微藻培養液通過採收單元進行採收,並回收培養液儲存槽中的培養液。接著,使用回收的培養液(稱為第二次培養液)進行第二次培養,於此回收的培養液中添加微藻所需營養液並生長5天後,此回收的培養液的濃度大約由0.25g/L生長至1.12g/L,重複上述採收與回收操作。然後,使用回收的培養液(稱為第三次培養液)進行第三次培養,於此回收的培養液中添加微藻所需營養液並生長5天後,此回收的培養液的濃度大約由0.25g/L生長至1g/L。在連續進行14天的培養與兩次微藻回收後,其生長折線圖如圖7所示。 The microalgae harvesting module of the above embodiment was used to carry out the harvesting of the microalgae. In this experimental example, three cultures were sequentially performed. During the experiment, the same ambient temperature, culture temperature, pH value of the culture solution and illumination were maintained, and the growth of the microalgae was detected according to the absorbance (OD) at 682 nm. First, in The culture medium containing the microalgae cells (referred to as the first culture solution) is added to the culture unit for the first culture, and after 4 days of culture, the microalgae cell concentration is increased from 0.2 g/L to 1.25 g/L, which includes The microalgae culture solution is recovered by the recovery unit, and the culture solution in the culture solution storage tank is recovered. Next, the second culture is carried out using the recovered culture solution (referred to as the second culture solution), and the nutrient solution required for the microalgae is added to the recovered culture solution and grown for 5 days, and the concentration of the recovered culture solution is approximately The above harvesting and recovery operations were repeated from 0.25 g/L to 1.12 g/L. Then, using the recovered culture solution (referred to as the third culture solution) for the third culture, the nutrient solution required for the microalgae is added to the recovered culture solution and grown for 5 days, and the concentration of the recovered culture solution is approximately Growth from 0.25 g/L to 1 g/L. After 14 days of continuous culture and two microalgae recovery, the growth line diagram is shown in Fig. 7.
由圖7中的生長折線圖,可知回收後的培養液可以適於循環再利用,以進行下一次培養、採收以及回收。因此,上述實施例的微藻採收模組具有實用性。 From the growth line graph in Fig. 7, it is understood that the recovered culture solution can be adapted for recycling for the next cultivation, harvesting, and recovery. Therefore, the microalgae harvesting module of the above embodiment has practicality.
綜上所述,本發明之微藻採收模組與微藻的採收方法中,藉由絮凝劑使微藻細胞與磁性粒子聚集成具有磁性的微藻磁性絮凝物,接著以施加磁場的方式來採收微藻磁性絮凝物。特別是,由於微藻磁性絮凝物會被磁力緊密地吸附於採收容器的內壁上,因此可以輕易且迅速地與採收容器內的培養液分離,進而得到具有緊密結構與低體積含水量的微藻磁性絮凝物。相較於習知使用絮凝劑的方法在藻體凝聚後,仍需搭配離心或過濾等方式去除剩餘的培養基或水份,本發明之微藻的採收方法可大幅縮短微 藻之採收時間與成本,使得採收之微藻細胞經過進一步的加工或是萃取可廣泛地應用於健康食品、生物餌料或做生質能源之原料等。 In summary, in the microalgae harvesting module and the microalgae harvesting method of the present invention, the microalgae cells and the magnetic particles are aggregated into the magnetic microalgae magnetic flocs by the flocculating agent, and then the magnetic field is applied. Ways to harvest microalgae magnetic floes. In particular, since the microalgae magnetic floc is strongly adsorbed by the magnetic force on the inner wall of the harvesting container, it can be easily and quickly separated from the culture liquid in the harvesting container, thereby obtaining a compact structure and a low volumetric water content. Microalgae magnetic flocs. Compared with the conventional method of using a flocculating agent, after the algae body is agglomerated, it is still necessary to remove the remaining medium or water by centrifugation or filtration, and the harvesting method of the microalgae of the present invention can be greatly shortened. The harvesting time and cost of algae enable the harvested microalgae cells to be widely used in health foods, biological baits or raw materials for biomass energy after further processing or extraction.
由於採收單元可以使用各種磁場裝置來提供磁場,以諸如直接設置或移除磁鐵或對電磁鐵供電與否的方式來輕易地調控磁場強度以及開啟或關閉磁場,故增加使用便利性。此外,採收單元在密閉式或是開放式環境下皆可進行。因此,採收單元可以輕易地與現有的養殖單元組合或併入養殖系統以形成微藻採收模組,且由於採收單元的尺寸大小可依據欲承接的培養槽之數量以及尺寸等參數而適當地進行調整,並無特別限制,因此亦有利於實施大規模的採收。更重要的是,磁性粒子的使用不會影響採收後微藻細胞之油脂萃取效率,且磁性粒子可再回收使用,以及與微藻磁性絮凝物分離的剩餘培養液仍可繼續進行下一批次之微藻養殖。因此,本發明提供低能耗、高採收率並具有水資源再利用的微藻採收模組與微藻的採收方法,能大幅降低微藻採收與養殖的操作成本,符合產業發展之需求。 Since the harvesting unit can use various magnetic field devices to provide a magnetic field, it is easy to adjust the magnetic field strength and turn the magnetic field on or off in such a manner as to directly set or remove the magnet or power the electromagnet, thereby increasing the convenience of use. In addition, the harvesting unit can be operated in a closed or open environment. Therefore, the harvesting unit can be easily combined with the existing breeding unit or incorporated into the breeding system to form the microalgae harvesting module, and since the size of the harvesting unit can be determined according to parameters such as the number and size of the culture tank to be subjected to. Appropriate adjustments are not particularly limited and are therefore beneficial for large-scale harvesting. More importantly, the use of magnetic particles does not affect the oil extraction efficiency of the microalgae cells after harvest, and the magnetic particles can be recycled, and the remaining culture solution separated from the microalgae magnetic floes can continue to the next batch. The second microalgae cultivation. Therefore, the present invention provides a microalgae harvesting module and a microalgae harvesting method with low energy consumption, high recovery rate and water resource reuse, which can greatly reduce the operating cost of microalgae harvesting and breeding, and is in line with industrial development. demand.
雖然本發明已以實施例揭露如上,然其並非用以限定本發明,任何所屬技術領域中具有通常知識者,在不脫離本發明的精神和範圍內,當可作些許的更動與潤飾,故本發明的保護範圍當視後附的申請專利範圍所界定者為準。 Although the present invention has been disclosed in the above embodiments, it is not intended to limit the present invention, and any one of ordinary skill in the art can make some changes and refinements without departing from the spirit and scope of the present invention. The scope of the invention is defined by the scope of the appended claims.
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