A7 B7 440422 五、發明説明（1.) a* (請先閲讀背面之注意事項再填寫」. 本發明係關於一種用於執行光化學、光催化反應及光 引發處理之裝置，尤係關於向光有機體及繁殖細胞之培養， 如微藻類等。 習知之用於培養向光有機體及繁殖細胞如微讓類等之 裝置’不是設計為了員層呈開放式、且置於戶外之水池形式， 便單獨由人造光源驅動，而其係以輸送導管來傳送培養媒 介。大部份含槽狀反應器之裝置，係為循環培養媒介之儀 器而備置，以達到所需程度之輻射強度，而其中該構造之 複雜性，會增加额外的費用《» 此開放式水池之設計會帶來污染的連續危險，以致不 可能純淨地培養。由於其所在地之氣候條件，此種裝置的 溫度調節亦十分困難。 在US-PS 4,473,970中指出一種以人造光為動力之裝 置，其培養媒介係被抽動而通過輸送導管。此種裝置之缺 點為，只能夠粗淺地見到幫浦及光能的動力消耗。 經濟部中央揉率為員工消费合作社印11 習知之其他裝置亦含有槽狀反應器，其光源係由光纖 電境來分配。光線之來源不是以環帶透鏡（Fresnel Lenses) 追隨日光軌跡，便及/或將人造光源射入同樣之光纖，以 照射培養媒介。此種裝置在製造及操作上均十分昂貴。 在US-PS 4,555,864中述及一種培養綠藻類之裝置，該 光纖係直接浸於培養槽内之培養媒介中，而其光能係由置 於上角之反射鏡導入。此種設備在設計上亦十分昂貴而繁 複。 在DE 41 34 813 A1中亦述及一種培養向光微生物之裝 本紙張尺度逋用中國囷家梂準（CNS ) A4规格（210X297公釐) -7- 經濟部中央橾率局貝工消費合作社印裝 4 4 04 2 2 A7 _______B7 _ 五、發明説明（2.) 置’其能夠不是以日光便及/或以人造光源來驅動，且通 過培養媒介流體。此種裝置之特徵為，一任意數量的小平 盤，彼此以等距相間隔，且置於兩塊平坦的平行透明板之 間，以一個液狀的緊實密封形成密室。在各個小平盤之末 端’有連接開口排列於調節密室，其中各個調節盤之連接 開口係經常置於相對的一端，以形成一條連續迂迴之通道， 在其前端密封’並在前後有通風口以作氣體交換。單由於 動力消耗之因素，此裝置便不適合用於工業階層之實施， 因為預設的高幫浦動力必須克服在連續迂迴狀之通道中的 流量阻力、及以此上述之小平盤為基礎裝備的高製造費用。A7 B7 440422 V. Description of the invention (1.) a * (Please read the notes on the back before filling in. "The present invention relates to a device for performing photochemical, photocatalytic reactions and photo-initiated treatment, especially to the Cultivation of photo organisms and reproductive cells, such as microalgae, etc. The conventional device for cultivating photo organisms and reproductive cells, such as micro lethals and the like, is not designed to be open to the crew, and placed in the form of outdoor pools, It is driven by an artificial light source alone, and it is used to transport the culture medium by a delivery catheter. Most of the devices containing a trough-shaped reactor are equipped for the circulation of the culture medium to achieve the required level of radiation intensity. The complexity of the structure will add additional costs. »The design of this open pool will bring a continuous danger of pollution, making it impossible to cultivate it purely. Due to the climatic conditions of its location, the temperature adjustment of this device is also very difficult. US-PS 4,473,970 indicates a device powered by artificial light, in which the culture medium is pumped through a delivery catheter. The disadvantage of this device is You can only see the power consumption of pumps and light energy in a superficial manner. The central unit of the Ministry of Economic Affairs is an employee consumer cooperative. 11 Other known devices also contain tank reactors, and the light source is distributed by the fiber optic environment. The source of light Instead of following the sunlight track with Fresnel Lenses, and / or shooting artificial light sources into the same optical fiber to illuminate the culture medium. Such devices are very expensive to manufacture and operate. It is described in US-PS 4,555,864 And a device for cultivating green algae, the optical fiber is directly immersed in the culture medium in the culture tank, and its light energy is introduced by a reflector placed at the upper corner. Such equipment is also very expensive and complicated in design. DE 41 34 813 A1 also describes a paper size for cultivating photomicroorganisms, using the Chinese Standard for Household Standards (CNS) A4 (210X297 mm) -7- Printed by the Shellfish Consumer Cooperative of the Central Bureau of the Ministry of Economic Affairs Equipment 4 4 04 2 2 A7 _______B7 _ V. Description of the invention (2.) The device can be driven not by sunlight and / or artificial light sources, but also by cultivating a medium fluid. The characteristics of this device are: The desired number of small flat plates are equidistantly spaced from each other and placed between two flat parallel transparent plates, forming a dense chamber with a liquid tight seal. At the end of each small flat plate, there are connection openings arranged to adjust In the closet, the connection openings of the various adjustment disks are often placed at opposite ends to form a continuous circuitous channel, sealed at the front end, and provided with vents in front and rear for gas exchange. Due to power consumption, this device It is not suitable for the implementation of the industrial class, because the preset high pump power must overcome the flow resistance in the continuous circuitous channel, and the high manufacturing cost based on the above-mentioned small flat plate.
Spektorova (1997年）述及導管狀之生物反應器的現 行狀況’其主要係使用於生產以醫藥工業及化妝品工業為 目的之生物活化物質。一個含有14立方公尺之培養體積、 且呈水平排列的玻璃導管生物反應器，係左烏茲別克斯坦 (Uzbekistan)所創》該玻璃導管生物反應器在速度大約2 t/annum時，以一最大生產率43 g/m2 · d來生產生物禮（綠 藻類）。 在此設計中，已在個別玻璃導管内之懸浮體分佈、系 統之溫度調整、及懸浮體内之極高含氧量中，找出問題範 園。此外，個別的水平玻璃導管裝配有輪形連接頭，會導 致其費用較高，且讓死的生物體及細菌得以有聚集之適當 位置。 根據Pulz (1992 a, b)實際上已完全附帶出管狀之玻 璃導管酵母（導管d為2.5公分）的操作，其中一個離心 本紙張尺度遺用中國国家揉準（CNS ) A4规格（210X297公釐> . ^------Ί裝------訂------線 (請先M.讀背面之注意事項再填寫.；) A7 B7 440422 五、發明説明（3.) 幫浦會迫使50升的藻類懸浮體成為一圏’圍繞於一光源。 取玻璃導管之遮蓋的表面區域為一培養的基準，然後此特 定區域之14 g πτβ1成長速率不超過前述之開放系統的生 產率。Spektorova (1997) described the current state of duct-like bioreactors', which is mainly used for the production of biologically activated substances for the pharmaceutical and cosmetic industries. A horizontally arranged glass tube bioreactor with a culture volume of 14 cubic meters, created by Uzbekistan. The glass tube bioreactor has a maximum productivity at a speed of about 2 t / annum. 43 g / m2 · d to produce bio-ceremonies (green algae). In this design, problem areas have been identified in the distribution of suspensions in individual glass ducts, the temperature adjustment of the system, and the extremely high oxygen content in the suspensions. In addition, individual horizontal glass conduits are equipped with a wheel-shaped connector, which results in higher costs and allows the dead organisms and bacteria to accumulate in place. According to the operation of Pulz (1992 a, b), the tube-shaped glass duct yeast (catheter d is 2.5 cm) has been completely attached. One of the centrifugal paper sizes is in accordance with China National Standard (CNS) A4 (210X297 mm). >. ^ ------ Outfitting ------ Order ----- (please M. read the notes on the back before filling in .;) A7 B7 440422 V. Description of the invention (3 .) The pump will force 50 liters of algae suspension to become a 'circle around a light source. Take the surface area covered by the glass duct as a reference for culture, and then the growth rate of 14 g πτβ1 in this specific area does not exceed the aforementioned opening System productivity.
Miyamoto等人（1卵8年）採用一種極昂贵的方法， 其中係在垂直站立且直徑d為5公分（表面積/體積比為 80 m-1)、2公尺高的玻璃導管中，培養微藻類，而該玻璃 導管係一種由螢光工業量產的產品β設立大量的平行導管 ’可以不費力地調整比例，但此種收集已證實是困難的， 以及當使用自然光源時，會出現不少加熱上的問題《最高 生產率係與培養之形態有關，介於含Nostoc氰基菌0.3 gl·1 、以及至多含Monoraphidium綠藻類0.6 gT1 d·1之間。 Jiittner (1977年）利用安裝一個额外的、冷卻循環液 所通過的内管’並進一步降低懸浮體内之深色體積，解決 了加熱上的問題。其以一個1.5的因子，測量所產生額外 之生長加速度。不論其技術複雜性及該計劃中之生存能力 的比例調整受到限制，仍可作為具有逆流冷卻器之若干開 放式空氣導管之裝置的模型（例如FR-PS 2 564 854)。 所有圓筒狀反應器之特徵為，在一個小表面積對體積 之比例上，有相當高的輻射強度，以致為確保藻類細胞有 充足的光線’及為避免光線抑制，需要在高流體速度中操 作。其缺點為，強烈之擾流會產生相應的重力，導致大多 數微藻類物種有抗生產效應。再者，較大型設備之有效光 線只能夠困難地釋放出來，或只有在相當的技術努力及經 本紙張尺度通用中國固豕標準（CNS ) A4規格（210x297公羡) -9 _ • ，兵τ ** (讀先閱讀背面之注意事項再填寫*」 τ 經濟部中央標準局属工消費合作社印製 A7 ,1 止 04 2 2___ 五、發明説明（4·) 費下才有可能β 在此本發明之目的’係利用薄層原理來改良過去的設 備，以達到更有效率地生產微生物，尤係關於處理向光微 生物之培養，並在天然日光之最大利用及繁殖懸浮體之最 佳狀況下，獲得可長年作用之範圍，特別是在能量與材料 替代之處理、以及水力流體之條件中，實現微生物之最大 產能’並且同時完成周邊設備之有效相互作用，以達到最 佳的作用結果。 依據本發明，此項工作可由申請專利範圍第丨項中之 特徵來解決《本發明之有利結構則描述於申請專利範面第 2項至第14項》 依據本發明所呈現之設備’係為有效率地生產微生物， 其含有一個生物反應器、一個收集裝置、一個養份溶液/ 母溶液進料裝置，以及一個養份溶液處理裝置。 經濟部中央揉準局貴工消费合作.杜印装 該生物反應器含有光合作用及水力（擾流）作用之薄 層系統、一個進料及回收系統、一個支配槽、一個熱交換 器、一個系統幫浦、一個測量器、容器光線之定量及定性 調整媒介、及氣链注入及抽出之設備。一個光合作用及水 力（擾流）作用之薄層系統中，含有大量的連績導管、或 彼此相互重疊且相互平行排列之管筒，其入口及出口端透 過接頭及減少横截面之連接器，與一個調節式進料器及一 個調節式回收器相連接’以使薄層容器之相互重疊排列、 並減少橫截面的各個連接器有一個橫截面，其可使一個均 勻之流體輪廓通過所有的薄層容器。 (CNS ) Α4规格（210X297公着） •10- A7 B7 44 04 2 2 _ -- 五、發明説明（5.) =本發明另一個特別之特徵減少橫截面之連接器， '疋、有:個在調節式進料器之流链方向增加之橫截面， 及/或是具有-個在_式回·之流體方向減少之橫 哉面。 々依據本發明―項進―步之特徵，此調節式進料器及調 節式回收器，各含有一條導管。 若凋節式進料器在流體方向有較小的直徑，而若調節 式回收器在流體方向有較大的直徑，則是相當有利的。 依據本發明一項進一步之特徵，穿透性之薄層容器含 有支配擾流器，以確保甚且在低流體速度、流體受擾齓時， 尚可提高表面積對基礎區域之比例、在穿透性之薄層容器 中提供撞擊光線之最佳分佈，以懸浮體中之潔淨微粒可將 容器表面有效地淨化’以防止任何可能發生於其上之固著 狀況’在其中設計有支配擾流器，以致在穿透性之薄層容 器中’沒有水力之靜止空間。 依據本發明一項進一步之特徵，此穿透性之薄層容器 含有至少一個玻璃導管之單位玻璃導管，彼此相互重疊排 列，並在破璃導管之生產期間與支配擾流管接合。 依據本發明其中一項較佳之構造，玻璃導管之全長係 由個別導管長所構成，不是膠黏便是焊接在一起，沒有任 何的水力干擾。 本發明其中一項較佳之構造為，容器光線之定量及定 性調整媒介，含有紫外線之螢光性、及/或反射性及/或 抗反射性、及/或穿透性材質，對於照射薄層容器中之微 本紙張尺度通用中國國家橾準（CNS ) A4规格（2l〇X297公釐） -11 - L；--：-----—裝------訂------線 (請先閩讀背面之注意事項再填寫本更) 經濟部中央標準局員工消费合作社印氧 440^22 五、發明説明（6.) 生物，可增加光合作用範圍内可取得之光線量。 在此例中之優點為，穿透性薄層容器之表面及/或壁 面材質，係由紫外線之螢光性及/或抗反射性材質所製成’ 對於照射薄層容器中之微生物’可增加光合作用範園内可 取得之光線量，及/或此紫外線之螢光性及穿透性材質係 置於薄層容器之間，及/或此紫外線之螢光性及穿透性材 質係置於薄層容器之下。 依據本發明一項造一步之特徵’用於調整容器光線之 定量及定性之媒介，含有紅外線之反射性及/或穿透性材 質，並於此穿透性薄層容器之表面或壁面材質整合，其使 穿透性薄層容器之壁面材質有效抵抗任何懸浮體中溫度的 增加，並提供繁殖懸浮體之輻射冷卻。 在本發明的理念中，氣體注入及移除之設備無論置於 地板内或地板上，都含有控溫之回收收集器，以將二氧化 碳注入繁殖懸浮體、將氧氣移出繁殖懸浮體，以及一個在 回收收集器中之氣體分侔器。 此之優點是為氣體注入及移除之設備提供了潛熱之儲 存材料。 經濟部肀央樣率局貞工消费合作社印装 本發明一項格外優良之構造為，支配容器、熱交換器、 及氣體注入及移除之設備相互連接，並同時一起運作。 在此考量之優點為’氣體注入及移除之設備、尤其是 回收收集器，亦同時含有部份之熱交換器及/或支配容器， 並因而建立共同效應’以達成繁殖懸浮體之最佳狀況β 本發明進一步備置有一個收集裝置，其含有一個收集 本紙張尺度逍用中國國家揉準（CNS ) Α4规格（210X297公釐） -12- A7 B7 440422 五、發明説明（7.) 容器、一個收集幫浦、一個分離器、及—個生物體槽。 本發明亦備置有一個養份溶液/母溶液進料裝置，其 含有一個養份溶液幫浦、一個具挽拌器之母溶液幫浦、及 一個養份溶液槽。 依據本發明一項特別之特徵，收集裝置、及/或養份 溶液/母溶液進料裝置，有一個養份處理裝置’由收集裝 置分離出來之繁殖懸浮體可透過它轉入生物反應器，如同 來自養份溶液/母溶液進料裝置之養份溶液、及/或養份 溶液/母溶液’可直接且無污染地轉入生物反應器。 本發明亦有這樣的理念，即養份溶液處理裝置含有一 個機械式前濾器、及一個活性碳過濾器，其可過濾出受污 染之物質，同時並允許微藻類之養份毫無阻礙地通過。 本發明一項格外優良之構造為，收集裝置、養份溶液 /母溶液進料裝置及養份溶液處理裝置相互連接，並同時 一起運作。 本發明更詳盡之細節’以一些結構實例描述如下： 圖一為依據本發明之設計的各項裝置圖； 圖二為具有進料及回收器之的玻璃導管組件、及支配擾 流器； 圖三為具有回咚器之玻璃導管組件（側視圖）、及容器光 線之定量及定性調整媒介》 圖一表示一依據本發明之設計的各項裝置圖，其用於 有效率地生產向光有機禮及繁殖細胞，尤其是在光線作用 下之微藻類。 本紙張尺度適用中菌國家標準{ CNS > A4规格（210X297公釐) -13 - .—：---;-----f 装------訂------線 (请先聞讀背面之注意事項再填寫本負) 經濟部中央標準局w工消費合作社印*. A7 B7 五、發明説明（8.) 本裝置含有一個生物反應器1、收集裝置2、一個養份 溶液/母溶液進料裝置3、及一個養份溶液處理裝置4 » 圖一中，將一種養份溶液灌於微生物，以生產一種繁 殖懸浮體/母溶液。裝置3起先含有一個養份溶液槽3a、 一個養份溶液幫浦3b、及一個具挽拌器之母溶液槽3c。 將養份溶液la由此直接導入生物反應器1中。在此實 例中’生物反應器1起先含有四個組件，一個光合作用及 水力作用之薄層系統la，其形成反應容器、一個進料及回 收系統分別為lb及lc、一個支配槽Id、一個熱交換器le、 一個系統幫浦If、一條測量線lg、反應容器光線之定量及 定性調整媒介lh及li (見囷二及圖三）、及氣體注入及移 除之設備。在此實例敘述中，此氣體注入及移除之設備， 含有一個在此實例中置於裝置底部的回收收集器lj、將二 氧化碳注入於回收收集器lj中的繁殖懸浮體之設備（未顯 示）、一個氧氣移除之設備Ik、及一個氣體分佈器11 (圖 三）。 一個氣體分佈器11置於回收收集器lj，其中此氣體分 佈器11將笔度25%之二氧化碳排氣，進入回收收集器lj 全長中之繁殖懸浮體。在此加熱需要有最高溫度攝氏38度 之排氣，並加熱繁殖懸浮體le。 一個熱交換器le可確保排氣及懸浮體維持在最佳溫 度。 為加強熱交換，此熱交換器le係安裝於系統幫浦If 之抽氣線上。二氧化碳排氣之承載狀況，係決定於pH值、 本紙柒尺度適用中國國家標準（CNS ) A4規格（210X297公釐） -14- ： 赛-- {請先閲讀背面之注意事項再填寫本爲) 訂. 線 經濟部中央標準局員工消費合作社印製 鎚濟部中央標準局I工消費合作杜印裝 44 0422 五、發明説明（9.) 繁殖懸淨體之溫度及光學密度，其係由系統繁浦If逆流之 測量線lg而測得。繁殖懸浮體及二氧化碳排氣之承載狀態 資料之測量、控制及儲存’係決定於一個中心測量、控制 及儲存單位（未顯示）。調整後之繁殖懸浮體，透過系統幫 浦If的一條幫浦線In，直接導入生物反應器1之光合作用 及水力作用之薄層系統la。在此實例中，薄層系統la含 有四個組件，其中每一組件係由大量彼此以等距相間隔、 相互重疊且相互平行排列之薄層容器（玻璃導管）1〇排列 而成，其入口及出口端透過接頭Ip及連接器lq，與一個 調節式進料器lr或調節式回收器is相連接各個連接器lq 分別有一個橫截面，其可使一個均勻之流體輪廓通過所有 的玻璃導管1〇。在此，連接器lq之該橫截面，在調節式 進料器lr之流體方向增加，反之，連接器lq之該橫截面 在調節式回收器之流體方向減少β調節式進料器及調節式 回收器lr及Is，各含有一個具接頭it以用於連接器iq的 導管，其中此調節.式進料器lr之橫截面，係在流體方向減 少，且調節式回收器Is之橫截面，係在流體方向增加。實 際的連接器lq之橫截面減少或增加、及調節式進料器及調 即式回收器的橫截面減少或增加，均能夠達到一個均句之 流體輪廓，以通過所有的薄層容器1〇。薄層容器丨〇亦備 置有許多支配擾流器1U，其甚至在低流體速度時，建立擾 流狀況、及增加表面積對基礎區域之比例，並確保在薄層 容器中撞擊光線之最佳分佈，以懸浮體中之潔淨微粒來避 免或排除任何發生於容器表面之固著狀況β 本紙張尺度適用tS®家縣（CNS ) Α4祕（210X297公釐) — --- I.!----------h 裝------訂------線 (請先M讀背面之注意事項再填寫本w ) ~ 15- 經濟部中央標準局員工消费合作杜印製 A7 ____B7_ 五、發明説明（10 ·) 在此提出之實例中，薄層系統la係由四個玻璃導管組 件而組成’每一個各含有一個由大量導管固定架排列於兩 侧、並互支#的骨架lv，其中導管1〇位於另一個之上， 並相互支撐。導管1〇之表面材質及/或避面材質、及/或 骨架lv或導管固定架（未顯示）、及/或置於薄層系統ia 上之基礎區域所配置之介質，含有特別的紫外線之螢光性、 及/或穿透性、及/或反射性材質，以達成反應容器lh及 li光線之定量及定性調整。如此對於照射薄層容器中之微 生物，可增加光合作用範圍内可取得之輻射量《此媒介可 能亦含有紅外線之反射性及/或穿透性材質，其可有效抵 抗懸浮體之溫度增加，並提供繁殖懸浮體之輻射冷卻，通 過穿透性薄層容器之壁面材質》在薄層系統la之生物體成 長的例子中，高能量之碳氫分子被建立。當繁殖懸浮體中 之乾燥體的濃度值大於2g/l時，可收集生物體》 然後此系統幫浦If使用於導引繁殖懸浮體進入收集裝 置2。其含有一個收集槽2a、一個收集幫浦2b、一個分離 器2c、及一個生物體槽2d。此分離器2c將生物體由養份 溶液中分離出來，隨後其不是導入養份溶液處理裝置4， 便及/或導入養份溶液/母溶液進料裝置3。 裝置4含有一個機械式前濾器（未顯示）、及一個活性 碳過濾器4a，其在允許微藻類之養份不受阻礙地通過時’ 將污染物質濾出。 以此製法所獲得之生物體，隨後導入一個處理裝置（未 顯示），在生產化學及/或藥物學基本材料及活性物質、及 (請先閲讀背面之注意事項再填寫本负) •裝. 訂 本纸張尺度通用中國®家摞準（CMS〉A4規格（2丨0X297公釐） -16- A7 B7 440422 五、發明説明（11.) /或高品質紙漿或紙漿添加物上，此高能量之碳氫分子可 被生產作為燃料使用。 經濟部中央標準局勇工消費合作社印裝 (請先閱讀背面之注意事項再填寫本頁) 本紙蒗尺度適用中國國家標準（CNS ) A4规格（2ίΟΧ297公釐） -17-Miyamoto et al. (1 year and 8 years) used an extremely expensive method, in which a micrometer was cultured in a glass tube standing vertically with a diameter d of 5 cm (surface area / volume ratio 80 m-1) and a height of 2 m. Algae, and the glass tube is a product produced by the fluorescent industry, which has a large number of parallel tubes' can be adjusted effortlessly, but this collection has proven difficult, and when natural light sources are used, the The problem of less heating "The highest productivity is related to the morphology of the culture, between 0.3 gl · 1 of Nostoc cyanobacteria and 0.6 gT1 d · 1 of Monoraphidium green algae at most. Jiittner (1977) solved the problem of heating by installing an additional inner tube 'through which the cooling fluid passed, and further reducing the dark volume in the suspension. It measures the additional growth acceleration produced by a factor of 1.5. Regardless of its technical complexity and the limited proportion of survivability in the program, it can still be used as a model for several open air duct devices with counterflow coolers (eg FR-PS 2 564 854). All cylindrical reactors are characterized by a relatively high radiation intensity in a small surface area to volume ratio, so that to ensure that algae cells have sufficient light, and to avoid light suppression, they need to be operated at high fluid speeds . The disadvantage is that the strong turbulence will generate corresponding gravity, which causes most microalgae species to have anti-production effects. In addition, the effective light of larger equipment can only be released with difficulty, or only with considerable technical effort and the standard of the Chinese standard (CNS) A4 (210x297) -9 _ •, bing τ * * (Read the precautions on the back before you fill in * ”τ Printed by the Central Standards Bureau of the Ministry of Economic Affairs and printed by A7, 1 to 04 2 2___ V. Description of the invention (4 ·) Only possible under the fee β In this invention The purpose of 'is to use the thin-layer principle to improve the past equipment to achieve more efficient production of microorganisms, especially regarding the treatment of the cultivation of light microorganisms, and under the best conditions of the maximum use of natural sunlight and the reproduction of suspensions, To obtain a range that can be used for many years, especially in the treatment of energy and material replacement, and the conditions of hydraulic fluids, to achieve the maximum production capacity of microorganisms and to complete the effective interaction of peripheral equipment at the same time to achieve the best effect. Invention, this work can be solved by the features in the scope of the patent application, "the advantageous structure of the invention is described in the patent application scope of the second item To item 14 "The apparatus presented according to the present invention is an efficient microorganism production, which includes a bioreactor, a collection device, a nutrient solution / master solution feeding device, and a nutrient solution processing device The Central Ministry of Economic Affairs of the Central Bureau of Guizhou Bureau of expensive labor and consumer cooperation. Du Yin installed the bioreactor contains photosynthesis and hydraulic (turbulent) thin layer system, a feed and recovery system, a control tank, a heat exchanger, A system pump, a measuring device, a quantitative and qualitative adjustment medium for container light, and a device for gas chain injection and extraction. A thin-layer system with photosynthesis and hydraulic (turbulent) action contains a large number of continuous pipes, Or the tubes that overlap each other and are arranged in parallel with each other, the inlet and outlet ends of the tubes are connected to an adjustable feeder and an adjustable recycler through joints and reduced cross-section connectors to make thin-layer containers mutually Each connector that is aligned and reduced in cross-section has a cross-section that allows a uniform fluid profile to pass through all thin layers (CNS) A4 specification (210X297) • 10- A7 B7 44 04 2 2 _-V. Description of the invention (5.) = Another special feature of the invention is to reduce the cross-section of the connector, '疋, 有: A cross section that increases in the direction of the flow chain of the adjustable feeder, and / or has a cross section that decreases in the direction of the fluid flow in the 式 -type return. 々 According to the feature of the "item advancement" step of the present invention, This regulating feeder and regulating recoverer each contain a duct. If the wither feeder has a smaller diameter in the fluid direction, and if the regulating recoverer has a larger diameter in the fluid direction, it is Very advantageous. According to a further feature of the invention, the penetrating thin-layer container contains a dominating spoiler to ensure that the ratio of the surface area to the base area can be increased even at low fluid speeds and fluid disturbances 2. Provide the best distribution of impinging light in the penetrating thin-layer container. The clean surface of the container can effectively purify the surface of the container 'to prevent any fixing conditions that may occur on it'. Dominates the spoiler so that it penetrates The container sheet are 'no still water of the space. According to a further feature of the present invention, the penetrating thin-layer container contains at least one unit glass tube of glass tubes, which are arranged on top of each other and are engaged with the dominant spoiler during the production of the broken glass tube. According to one of the preferred structures of the present invention, the entire length of the glass tube is composed of individual tube lengths, either glued or welded together without any hydraulic interference. One of the preferred structures of the present invention is a quantitative and qualitative adjustment medium for container light, containing ultraviolet fluorescent and / or reflective and / or anti-reflective and / or transmissive materials. The micro-paper size in the container is generally in accordance with China National Standards (CNS) A4 specifications (210 × 297 mm) -11-L;-: ------- packing ------ order ---- --Line (please read the precautions on the back before filling out this change) Employees of the Central Standards Bureau of the Ministry of Economic Affairs Consumption Cooperative Printed Oxygen 440 ^ 22 V. Description of the Invention (6.) Biological can increase the light available in the photosynthesis range the amount. The advantage in this example is that the material of the surface and / or wall of the penetrating thin-layer container is made of ultraviolet-fluorescent and / or anti-reflective material. Increase the amount of light that can be obtained in the photosynthesis range, and / or the fluorescent and transmissive material of this ultraviolet light is placed between thin containers, and / or the fluorescent and transmissive material of this ultraviolet light is placed Under the thin container. According to a further feature of the present invention, a medium for adjusting the quantitative and qualitative properties of container light, which includes infrared reflective and / or transmissive materials, and integrates the surface or wall material of the transmissive thin-layer container It makes the wall material of the penetrating thin-layer container effective against any increase in temperature in the suspension, and provides radiant cooling of the reproduction suspension. In the concept of the present invention, whether the gas injection and removal equipment is placed in or on the floor, it contains a temperature-controlled recovery collector to inject carbon dioxide into the breeding suspension, remove oxygen from the breeding suspension, and Recovery of gas decanter in the collector. This has the advantage of providing a latent heat storage material for gas injection and removal equipment. Printed by Zhengong Consumer Cooperative of the Ministry of Economic Affairs Bureau of the Central Government A particularly good structure of the present invention is that the devices that control the container, heat exchanger, and gas injection and removal are connected to each other and operate together at the same time. The advantage considered here is that 'the gas injection and removal equipment, especially the recovery collector, also contains part of the heat exchanger and / or the control container, and thus establishes a common effect' to achieve the best breeding suspension Condition β The present invention is further provided with a collecting device, which contains a paper collection standard for Chinese papers (CNS) A4 specification (210X297 mm) -12- A7 B7 440422 V. Description of the invention (7.) Container, A collection pump, a separator, and a biological tank. The present invention is also provided with a nutrient solution / master solution feeding device, which contains a nutrient solution pump, a mother solution pump with a stirrer, and a nutrient solution tank. According to a special feature of the present invention, the collection device, and / or the nutrient solution / mother solution feeding device, has a nutrient processing device 'the breeding suspension separated by the collection device can be transferred to the bioreactor through it, The nutrient solution, and / or the nutrient solution / mother solution ', as from a nutrient solution / master solution feeding device, can be transferred directly and without pollution into the bioreactor. The invention also has the idea that the nutrient solution processing device contains a mechanical pre-filter and an activated carbon filter, which can filter out contaminated substances and allow microalgae nutrients to pass through without hindrance . A particularly excellent structure of the present invention is that the collection device, the nutrient solution / mother solution feeding device, and the nutrient solution processing device are connected to each other and operate together at the same time. The more detailed details of the present invention are described below with some structural examples: FIG. 1 is a diagram of various devices designed according to the present invention; FIG. 2 is a glass tube assembly with a feed and recovery device, and a dominating spoiler; The third is a glass tube assembly (side view) with a retort, and a quantitative and qualitative adjustment medium for the container light. Figure 1 shows a diagram of various devices designed according to the present invention, which is used to efficiently produce organic light. Ceremony and reproduction cells, especially microalgae under light. This paper size is applicable to the National Standard for Chinese Bacteria {CNS > A4 specification (210X297 mm) -13-.—: ---; ------------------- (Please read the precautions on the back before filling in the negative) Printed by the Central Standards Bureau of the Ministry of Economic Affairs and Industrial Cooperatives Cooperatives *. A7 B7 V. Description of the Invention (8.) This device contains a bioreactor 1, a collection device 2, and a Nutrient solution / master solution feeding device 3 and a nutrient solution processing device 4 »In Figure 1, a nutrient solution is poured into a microorganism to produce a reproduction suspension / master solution. The device 3 initially contains a nutrient solution tank 3a, a nutrient solution pump 3b, and a mother solution tank 3c with a stirrer. The nutrient solution 1a is thus directly introduced into the bioreactor 1. In this example, the 'bioreactor 1 first contains four components, a thin layer system la of photosynthesis and hydraulic action, which forms a reaction vessel, a feeding and recovery system are lb and lc, a control tank Id, a Heat exchanger le, a system pump If, a measurement line lg, quantitative and qualitative adjustment media lh and li of the reaction vessel light (see Figures 2 and 3), and equipment for gas injection and removal. In this example description, the gas injection and removal equipment includes a recovery collector lj placed in the bottom of the device in this example, and a device (not shown) for injecting carbon dioxide into the reproduction suspension lj in the recovery collector lj. , An oxygen removal device Ik, and a gas distributor 11 (Figure 3). A gas distributor 11 is placed in the recovery collector lj, wherein the gas distributor 11 exhausts 25% of carbon dioxide into the breeding suspension in the entire length of the recovery collector lj. The heating here requires an exhaust gas with a maximum temperature of 38 ° C and heating the breeding suspension le. A heat exchanger le ensures that the exhaust and suspension are maintained at the optimum temperature. To enhance heat exchange, this heat exchanger le is installed on the exhaust line of the system pump If. The carrying condition of carbon dioxide exhaust is determined by the pH value and the paper size. The Chinese National Standard (CNS) A4 specification (210X297 mm) is applicable. -14- ： --- Please read the precautions on the back before filling in this. Order. Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economics and Industry I. Industrial and consumer cooperation of the Central Standards Bureau of the Ministry of Industry Du Yinzhuang 44 0422 5. Description of the invention (9.) The temperature and optical density of the breeding suspension are determined by the system It is measured by the measurement line lg of Fanpu If countercurrent. Carrying state of breeding suspension and carbon dioxide exhaust gas The measurement, control and storage of data 'is determined by a central measurement, control and storage unit (not shown). The adjusted breeding suspension is directly introduced into the bioreactor 1's photosynthesis and hydraulic thin-layer system la through a pump line In of the system pump If. In this example, the thin layer system la contains four components, each of which is formed by a large number of thin layer containers (glass ducts) 10 spaced from each other at equal intervals, overlapping each other, and arranged in parallel with each other, and its entrance And the outlet end is connected with an adjustable feeder lr or an adjustable recycler is through a joint Ip and a connector lq. Each connector lq has a cross section, which allows a uniform fluid profile to pass through all the glass ducts. 1〇. Here, the cross section of the connector lq increases in the fluid direction of the regulating feeder lr, and conversely, the cross section of the connector lq decreases in the fluid direction of the regulating recoverer β regulating feeder and regulating The recoverer lr and Is each contain a conduit with a joint it for the connector iq, in which the cross section of the adjusting type feeder lr is reduced in the direction of the fluid, and the cross section of the adjusting type recoverer Is, The system increases in fluid direction. The decrease or increase of the cross-section of the actual connector lq, and the decrease or increase of the cross-section of the adjustable feeder and the adjustable type recycler can all reach a uniform fluid profile to pass through all the thin-layered containers1. . Thin-layer vessels are also equipped with a number of dominating spoilers 1U, which establish turbulence conditions and increase the ratio of surface area to the base area even at low fluid velocities, and ensure the best distribution of impinging light in thin-layer vessels To avoid or exclude any fixation on the surface of the container with clean particles in the suspension β This paper size is suitable for tS® home county (CNS) Α4 secret (210X297 mm) — --- I.! --- ------- h install ------ order ------ line (please read the notes on the back before filling in this w) ~ 15- Consumption cooperation of employees of the Central Standards Bureau of the Ministry of Economic Affairs System A7 ____B7_ V. Description of the Invention (10 ·) In the example presented here, the thin-layer system la is composed of four glass catheter assemblies. Each one contains a large number of catheter holders arranged on both sides and supporting each other. The skeleton lv of #, in which the catheter 10 is located on the other and supports each other. The surface material and / or avoiding material of the catheter 10, and / or the skeleton lv or the catheter holder (not shown), and / or the medium arranged in the base area on the thin-layer system ia, contains special ultraviolet rays. Fluorescent, and / or transmissive, and / or reflective materials to achieve quantitative and qualitative adjustment of the reaction vessel lh and li light. In this way, for irradiating microorganisms in thin-layer containers, the amount of radiation that can be obtained within the photosynthesis range can be increased. This medium may also contain infrared reflective and / or penetrating materials, which can effectively resist the temperature increase of the suspension, and Provides radiative cooling of the breeding suspension, through the wall material of the penetrating thin-layer container. In the example of the growth of organisms in the thin-layer system la, high-energy hydrocarbon molecules are established. When the concentration of the dried body in the breeding suspension is greater than 2 g / l, the organism can be collected. The system then uses If to guide the breeding suspension into the collection device 2. It contains a collection tank 2a, a collection pump 2b, a separator 2c, and a biological tank 2d. This separator 2c separates the organism from the nutrient solution, and then it is not introduced into the nutrient solution processing device 4, and / or the nutrient solution / mother solution feeding device 3 is introduced. The device 4 contains a mechanical front filter (not shown), and an activated carbon filter 4a, which filters out contaminants while allowing microalgae nutrients to pass unhindered. The organisms obtained by this method are then introduced into a processing device (not shown) to produce basic chemical and / or pharmacological materials and active substances, and (please read the precautions on the back before filling in this burden) • equipment. The size of the paper is GM China® Standard (CMS> A4 (2 丨 0X297mm) -16- A7 B7 440422 V. Description of the invention (11.) / or high-quality pulp or pulp additives, this high Hydrocarbon molecules of energy can be produced and used as fuel. Printed by Yonggong Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs (please read the notes on the back before filling out this page). Mm) -17-