TW201801786A - Treatment method for reducing carbon dioxide emissions by using microalgae culture to reduce the emission of carbon dioxide for waste water - Google Patents

Treatment method for reducing carbon dioxide emissions by using microalgae culture to reduce the emission of carbon dioxide for waste water Download PDF

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TW201801786A
TW201801786A TW105122028A TW105122028A TW201801786A TW 201801786 A TW201801786 A TW 201801786A TW 105122028 A TW105122028 A TW 105122028A TW 105122028 A TW105122028 A TW 105122028A TW 201801786 A TW201801786 A TW 201801786A
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aqueous solution
carbon dioxide
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weakly acidic
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TWI626982B (en
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林正仁
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Abstract

The present invention relates to a treatment method of reducing carbon dioxide emissions with high efficiency. The method comprises the following steps of: absorbing exhaust gas containing carbon dioxide by using an alkaline aqueous solution having a concentration lower than 20 weight percentage to obtain a weakly acidic aqueous solution rich in carbonate ions and bicarbonate ions; utilizing the characteristics of photosynthesis carbon fixation of microalgae to add the weakly acidic aqueous solution to the microalgae culture tank to provide the carbon source needed for microalgae photosynthesis. The present invention effectively absorbs carbon dioxide by an alkaline aqueous solution, and then uses the microalgae culture for photosynthesis to solve the problems of ineffectiveness in poor absorption of carbon dioxide by fresh water or seawater, and environmental pollution caused by the direct discharge of waste water, thereby effectively reducing the emission of carbon dioxide.

Description

降低二氧化碳排放量之處理方法Treatment methods to reduce carbon dioxide emissions

本發明係關於一種廢氣之淨化處理方法,尤指一種降低廢氣中二氧化碳排放量之處理方法。The present invention relates to a method for purifying exhaust gas, and more particularly to a method for reducing carbon dioxide emissions in exhaust gas.

由於人類大量發展工業排放溫室氣體,造成全球暖化問題日益嚴重,全球溫度不斷上升,已足以影響全球物種生存關鍵,因此如何減少溫室氣體之排放已是全球共同的目標。目前已發展出各種減少二氧化碳排放之解決方法,諸如提高燃料效率或二氧化碳捕捉吸附等,相關專利有TW201100532、TW201317045等。Due to the large amount of industrial development of greenhouse gas emissions, the global warming problem is becoming increasingly serious, and the continuous rise in global temperature is enough to affect the survival of global species. Therefore, how to reduce greenhouse gas emissions has become a common goal worldwide. Various solutions have been developed to reduce carbon dioxide emissions, such as improving fuel efficiency or carbon dioxide capture and adsorption. Related patents include TW201100532 and TW201317045.

於現有技術中,降低二氧化碳含量之方式係使用淡水或海水為沖洗劑,利用水洗技術沖洗含有二氧化碳之廢氣,從而設法令部分二氧化碳氣體溶解於淡水或海水中。然而,如Journal of Chemical and Engineering Data ,1970, 15 (1) , p 67-p 71所述,二氧化碳氣體於25° C、20大氣壓下每100公克淡水中僅能溶2.403公克二氧化碳,且二氧化碳氣體於25° C、1大氣壓下每100公克海水中僅能溶0.11公克二氧化碳,故不論使用淡水或海水沖洗廢氣皆難以獲得預期的水洗效果,而且水洗後所產生之碳酸水若未經過處理直接排放至河川或海水中,亦會引起環境酸化汙染。In the prior art, a method of reducing carbon dioxide content is to use fresh water or seawater as a flushing agent, and use water washing technology to flush exhaust gas containing carbon dioxide, so as to try to dissolve part of the carbon dioxide gas in the freshwater or seawater. However, as described in Journal of Chemical and Engineering Data , 1970, 15 (1) , p 67-p 71, carbon dioxide gas can only dissolve 2.403 grams of carbon dioxide per 100 grams of fresh water at 25 ° C and 20 atmospheres, and the carbon dioxide gas Only 0.11 grams of carbon dioxide can be dissolved per 100 grams of seawater at 25 ° C and 1 atmosphere, so it is difficult to obtain the desired washing effect regardless of whether the fresh water or seawater is used to flush the exhaust gas, and the carbonated water produced after washing is directly discharged without treatment To rivers or seawater, it will also cause environmental acidification pollution.

有鑑於現有技術存在之技術缺陷,本發明之目的在於改善一般淡水或海水吸收二氧化碳的效果不彰以及廢水直接排放而造成環境汙染之問題,進而高效地減少二氧化碳之排放量。In view of the technical shortcomings of the prior art, the purpose of the present invention is to improve the problem of ineffective carbon dioxide absorption in general freshwater or seawater and the environmental pollution caused by the direct discharge of wastewater, thereby efficiently reducing the amount of carbon dioxide emissions.

為達成前述目的,本發明提供一種降低二氧化碳排放量之處理方法,其包含以下步驟:收集含有二氧化碳之廢氣;以濃度低於20重量百分比之鹼性水溶液吸收所述廢氣中的二氧化碳,並得一弱酸性水溶液,所述弱酸性水溶液中含有碳酸根離子、碳酸氫根離子與金屬離子;以及將該弱酸性水溶液加入含有微藻之微藻養殖槽中進行光合作用,藉以降低弱酸性水溶液中碳酸根離子及碳酸氫根離子的濃度,以得到一經處理的廢水。To achieve the foregoing object, the present invention provides a treatment method for reducing carbon dioxide emissions, which includes the following steps: collecting exhaust gas containing carbon dioxide; absorbing carbon dioxide in the exhaust gas with an alkaline aqueous solution having a concentration of less than 20% by weight, and obtaining a A weakly acidic aqueous solution containing carbonate ions, bicarbonate ions, and metal ions; and adding the weakly acidic aqueous solution to a microalgae culture tank containing microalgae for photosynthesis, thereby reducing carbonic acid in the weakly acidic aqueous solution Concentration of root ions and bicarbonate ions to obtain a treated wastewater.

依據本發明,藉由使用濃度低於20重量百分比之鹼性水溶液之技術手段,能夠大幅改善現有技術使用淡水或海水吸收二氧化碳時效果不彰之問題,並可節省該鹼性水溶液之用水量,達到節約用水的效果。According to the present invention, the technical means of using an alkaline aqueous solution having a concentration of less than 20% by weight can greatly improve the problem of poor results when absorbing carbon dioxide using fresh water or seawater in the prior art, and can save water consumption of the alkaline aqueous solution. To achieve the effect of saving water.

更佳的,於前述收集含有二氧化碳之廢氣之步驟以及以濃度低於20重量百分比之鹼性水溶液吸收所述廢氣中的二氧化碳並得該弱酸性水溶液之步驟包括:收集含有二氧化碳之廢氣;對所述含有二氧化碳之廢氣進行前處理,獲得一經前處理之廢氣,該經前處理之廢氣含有二氧化碳;以濃度低於20重量百分比之該鹼性水溶液吸收該經前處理之廢氣中的二氧化碳,得到該弱酸性水溶液;其中,所述前處理為集塵處理、脫硫處理、脫硝處理、降溫處理或其組合。More preferably, the step of collecting the exhaust gas containing carbon dioxide and the step of absorbing the carbon dioxide in the exhaust gas with an alkaline aqueous solution having a concentration of less than 20% by weight to obtain the weakly acidic aqueous solution include: collecting the exhaust gas containing carbon dioxide; The exhaust gas containing carbon dioxide is pre-processed to obtain a pre-treated exhaust gas, the pre-treated exhaust gas contains carbon dioxide; the alkaline aqueous solution with a concentration of less than 20% by weight absorbs the carbon dioxide in the pre-treated exhaust gas to obtain the Weakly acidic aqueous solution; wherein the pretreatment is a dust collection treatment, a desulfurization treatment, a denitration treatment, a temperature reduction treatment, or a combination thereof.

較佳的,該鹼性水溶液為含有IA族元素金屬離子的水溶液、含有IIA族元素金屬離子的水溶液或其組合;更佳的,該鹼性水溶液為氫氧化鈉水溶液、氫氧化鈣水溶液、氫氧化鉀水溶液、氨水溶液或其組合;再更佳的,該鹼性水溶液為氫氧化鈉水溶液。Preferably, the alkaline aqueous solution is an aqueous solution containing a group IA element metal ion, an aqueous solution containing a group IIA element metal ion, or a combination thereof; more preferably, the alkaline aqueous solution is a sodium hydroxide aqueous solution, a calcium hydroxide aqueous solution, hydrogen An aqueous potassium oxide solution, an aqueous ammonia solution, or a combination thereof; even more preferably, the alkaline aqueous solution is an aqueous sodium hydroxide solution.

較佳的,該鹼性水溶液之濃度係低於或等於10重量百分比;更佳的,該鹼性水溶液之濃度係高於或等於3重量百分比且低於或等於5重量百分比;再更佳的,該鹼性水溶液之濃度係高於或等於3重量百分比且低於或等於3.5重量百分比。Preferably, the concentration of the alkaline aqueous solution is less than or equal to 10% by weight; more preferably, the concentration of the alkaline aqueous solution is greater than or equal to 3% by weight and less than or equal to 5% by weight; even more preferably The concentration of the alkaline aqueous solution is higher than or equal to 3 weight percent and lower than or equal to 3.5 weight percent.

較佳的,該弱酸性水溶液之酸鹼值大於或等於5且小於或等於7。更佳的,該弱酸性水溶液之酸鹼值大於或等於5且小於或等於6。Preferably, the weakly acidic aqueous solution has a pH value of 5 or more and 7 or less. More preferably, the weakly acidic aqueous solution has a pH value of 5 or more and 6 or less.

較佳的,該微藻為葡萄藻(Botryococcus braunii )、小球藻(Chlorella sp. )、隱甲藻(Crypthecodinium cohnii )、細柱藻(Cylindrotheca sp. )、杜氏藻(Dunaliella primolecta )、等鞭金藻(Isochrysis sp. )、單腸藻(Monalanthus Salina )、微小綠藻(Nannochloris sp. )、擬球藻(Nannochloropsis sp. )、新綠藻(Neochloris oleoabundans )、菱形藻(Nitzschia sp. )、三角褐指藻(Phaeodactylum tricornutum )、裂殖壺菌(Schizochytrium sp.) 、司西扁藻(Tetraselmis suecica )或其組合。再更佳的,該微藻為利用海水養殖的小球藻、杜氏藻、等鞭金藻、微小綠藻、新綠藻、裂殖壺菌。Preferably, the microalgae are Botryococcus braunii , Chlorella sp. , Crypthecodinium cohnii , Cylindrotheca sp. , Dunaliella primolecta , etc. Isochrysis sp. , Monalanthus Salina , Nannochloris sp. , Nannochloropsis sp. , Neochloris oleoabundans , Nitzschia sp. , Phaeodactylum tricornutum , Schizochytrium sp. , Tetraselmis suecica , or a combination thereof. Even more preferably, the microalgae are chlorella, Dunaliella, Isochrysis, micro green algae, neo green algae, and Schizochytrium.

較佳的,該微藻養殖槽係一密閉式微藻養殖槽。相較於採用開放式微藻養殖槽,密閉式微藻養殖槽具有對於土地需求較低、較不受天氣變化影響等優點。因此,本發明之方法更具有微藻產能較高且穩定、固碳效率較高以及該微藻之藻脂含量較高等優點。Preferably, the microalga cultivation tank is a closed microalga cultivation tank. Compared with the use of open microalgae culture tanks, the closed microalgae culture tanks have the advantages of lower land demand and being less affected by weather changes. Therefore, the method of the present invention has the advantages of higher productivity and stability of microalgae, higher carbon fixation efficiency, and higher algal fat content of the microalgae.

更佳的,於前述將該弱酸性水溶液加入含有微藻之微藻養殖槽中進行光合作用,藉以降低弱酸性水溶液中碳酸根離子及碳酸氫根離子的濃度,以得到該經處理的廢水之步驟包括:將該弱酸性水溶液加入含有微藻之微藻養殖槽中進行光合作用,藉以降低弱酸性水溶液中碳酸根離子及碳酸氫根離子的濃度,獲得一第一處理溶液,該第一處理溶液之酸鹼值大於8;於該第一處理溶液中補入該弱酸性水溶液,獲得一第二處理溶液,該第二處理溶液之酸鹼值為大於或等於6且小於或等於7,所述第二處理溶液中含有碳酸根離子、碳酸氫根離子與金屬離子;於該含有微藻及該第二處理溶液之微藻養殖槽中,令微藻進行光合作用,藉以降低第二處理溶液中碳酸根離子及碳酸氫根離子的濃度,以得到該經處理的廢水。再更佳的,該微藻養殖槽係一全自動微藻養殖槽,其能根據所偵測到的第一處理溶液之酸鹼值、水流速度、溫度、藻密度、光照度等參數,在適當時機下,於第一處理溶液中自動化補入弱酸性水溶液,從而確保微藻養殖槽中的微藻能持續進行光合作用。More preferably, the weakly acidic aqueous solution is added to the microalgae-containing microalgae breeding tank for photosynthesis in order to reduce the concentration of carbonate ions and bicarbonate ions in the weakly acidic aqueous solution to obtain the treated wastewater. The steps include: adding the weakly acidic aqueous solution to a microalgae culture tank containing microalgae for photosynthesis, thereby reducing the concentration of carbonate ions and bicarbonate ions in the weakly acidic aqueous solution to obtain a first treatment solution, and the first treatment The acid-base value of the solution is greater than 8; the weakly acidic aqueous solution is added to the first treatment solution to obtain a second treatment solution, and the acid-base value of the second treatment solution is greater than or equal to 6 and less than or equal to 7, so The second treatment solution contains carbonate ions, bicarbonate ions and metal ions; in the microalga cultivation tank containing microalgae and the second treatment solution, the microalgae performs photosynthesis, thereby reducing the second treatment solution Concentration of carbonate ions and bicarbonate ions to obtain the treated wastewater. Even better, the microalgae breeding tank is a fully automatic microalgae culture tank, which can detect the pH value of the first treatment solution, water flow speed, temperature, algae density, and light intensity, etc. When the time comes, the weakly acidic aqueous solution is automatically replenished in the first treatment solution, thereby ensuring that the microalgae in the microalgae cultivation tank can continuously perform photosynthesis.

較佳的,於前述將該弱酸性水溶液加入含有微藻之微藻養殖槽中進行光合作用,藉以降低弱酸性水溶液中碳酸根離子及碳酸氫根離子的濃度,以得到該經處理的廢水之步驟之後包括:將所述經處理後的廢水進行後續處理,獲得一上清液與一含有微藻之藻泥沉澱物,所述上清液中含有氫氧根離子與金屬離子;以及對所述含有微藻之藻泥沉澱物進行乾燥處理,獲得一乾藻粉;其中,所述後續處理為沉澱處理、過濾處理或其組合。所述乾藻粉可直接應用於食品、飼料、肥料之原料或直接當成燃料使用。更佳的,所述濃度低於20重量百分比之鹼性水溶液為所述經處理的廢水進行後續處理所收集得到之上清液;且於前述以濃度低於20重量百分比之該鹼性水溶液吸收所述廢氣中的二氧化碳,並得該弱酸性水溶液之步驟包括:以該上清液吸收所述廢氣中的二氧化碳,並得該弱酸性水溶液。更佳的,所述之該上清液為濃度低於或等於5重量百分比之鹼性水溶液。更佳的,於前述對所述含有微藻之藻泥沉澱物進行乾燥處理,獲得該乾藻粉之步驟之後包括:將該乾藻粉利用破壁處理,取得一藻油及一藻塊;將該藻油轉酯處理,得一生質柴油。所述藻塊可作為動物飼料或肥料。Preferably, the weakly acidic aqueous solution is added to the microalgae-containing microalgae culture tank for photosynthesis, so as to reduce the concentration of carbonate ions and bicarbonate ions in the weakly acidic aqueous solution to obtain the treated wastewater. After the step, the treated wastewater is subjected to subsequent treatment to obtain a supernatant and a sediment of algae mud containing microalgae, wherein the supernatant contains hydroxide ions and metal ions; and The algae slime containing microalgae is dried to obtain a dried algae powder, wherein the subsequent treatment is a precipitation treatment, a filtration treatment, or a combination thereof. The dried algae powder can be directly applied to raw materials of food, feed, fertilizer or used directly as fuel. More preferably, the alkaline aqueous solution having a concentration of less than 20% by weight is a supernatant collected by subsequent treatment of the treated wastewater; and is absorbed by the alkaline aqueous solution having a concentration of less than 20% by weight as described above. The step of obtaining carbon dioxide in the exhaust gas to obtain the weakly acidic aqueous solution includes: absorbing carbon dioxide in the exhaust gas with the supernatant to obtain the weakly acidic aqueous solution. More preferably, the supernatant is an alkaline aqueous solution having a concentration of less than or equal to 5 weight percent. More preferably, after the aforesaid step of drying the algae slime containing microalgae to obtain the dried algae powder, the method comprises: using the wall breaking treatment of the dried algae powder to obtain an algae oil and an algae block; This algal oil is transesterified to obtain a biodiesel. The algae block can be used as animal feed or fertilizer.

依據本發明,所述將該乾藻粉用破壁處理,取得一藻油及一藻塊之步驟可採用超音波震盪破壁萃取法、電漿破壁萃取法或超臨界破壁萃取法完成,但並非僅限於此。依據本發明,所述將該藻油轉酯處理,得一生質柴油之步驟可採用氫氧化鈉鹼化反應法、高溫超臨界轉酯反應法或酵素催化轉酯反應法完成,但並非僅限於此。According to the present invention, the step of treating the dried algae powder by breaking the wall to obtain algae oil and algae block can be performed by ultrasonic vibration wall-breaking extraction method, plasma wall-breaking extraction method or supercritical wall-breaking extraction method. , But it's not limited to this. According to the present invention, the step of transesterifying the algal oil to obtain a biodiesel can be completed by a sodium hydroxide alkalinization reaction method, a high-temperature supercritical transesterification reaction method, or an enzyme-catalyzed transesterification reaction method, but it is not limited to this.

本發明之處理方法的優點在於:以濃度低於20重量百分比之鹼性水溶液大幅提高二氧化碳之溶解度,有效吸收二氧化碳,亦降低原先以淡水或海水為溶劑的水量;而該弱酸性水溶液中含有碳酸根離子、碳酸氫根離子與金屬離子,該弱酸性水溶液加入含有微藻之微藻養殖槽進行光合作用,使得微藻可加速利用該弱酸性水溶液中之碳酸根離子及碳酸氫根離子進行生物固碳。據此,本發明之技術手段能改善一般淡水或海水吸收二氧化碳效果不彰,以及其廢水直接排放而造成環境汙染之問題,達成高效減少二氧化碳排放量。The treatment method of the present invention has the advantages of greatly increasing the solubility of carbon dioxide with an alkaline aqueous solution having a concentration of less than 20% by weight, effectively absorbing carbon dioxide, and reducing the amount of water originally using fresh water or seawater as a solvent; and the weakly acidic aqueous solution contains carbonic acid Root ions, bicarbonate ions and metal ions, the weakly acidic aqueous solution is added to a microalgae culture tank containing microalgae for photosynthesis, so that the microalgae can accelerate the use of carbonate and bicarbonate ions in the weakly acidic aqueous solution for biological Carbon fixation. According to this, the technical means of the present invention can improve the problem of poor absorption of carbon dioxide by freshwater or seawater in general and the environmental pollution caused by the direct discharge of wastewater, thereby achieving a high efficiency in reducing carbon dioxide emissions.

依據本發明,1公斤之微藻約可吸收2.28公斤之二氧化碳,其成效遠比植樹淨化二氧化碳效果佳。此外,微藻養殖吸收二氧化碳同時亦可產出生質柴油供以作為能源,且藻塊可成為動物飼料或肥料,使得本發明中之產物皆能被有效運用。According to the present invention, one kilogram of microalgae can absorb about 2.28 kilograms of carbon dioxide, and its effect is far better than that of planting trees to purify carbon dioxide. In addition, the carbon dioxide absorbed by the microalgae cultivation can also produce biodiesel for energy, and the algae block can be used as animal feed or fertilizer, so that the products of the present invention can be effectively used.

請參閱圖1所示,首先,收集含有二氧化碳之廢氣,經由集塵、脫氮、脫硝、降溫處理後,排入二氧化碳吸收設備中,於二氧化碳吸收設備內,以含有濃度3.5重量百分比之氫氧化鈉水溶液,使用循環噴灑的方式吸收廢氣中的二氧化碳,得到含有碳酸根離子、碳酸氫根離子與鈉離子的碳酸氫鈉水溶液(即弱酸性水溶液)與經處理之廢氣。其中,該碳酸氫鈉水溶液之酸鹼值約為5至6。Please refer to FIG. 1. First, the exhaust gas containing carbon dioxide is collected, and after being treated by dust collection, denitrification, denitration, and temperature reduction, it is discharged into a carbon dioxide absorption device, and the carbon dioxide absorption device contains hydrogen at a concentration of 3.5% by weight. The sodium oxide aqueous solution absorbs carbon dioxide in the exhaust gas by using a cyclic spraying method to obtain an aqueous sodium hydrogen carbonate solution (ie, a weakly acidic aqueous solution) containing carbonate ions, bicarbonate ions, and sodium ions, and the treated exhaust gas. The pH value of the aqueous sodium hydrogen carbonate solution is about 5 to 6.

於此,藉由使用1000公斤濃度3.5重量百分比之氫氧化鈉水溶液可吸收38.5公斤之二氧化碳,於等量的廢氣中,經處理之廢氣中二氧化碳的含量自45 ppm降為0.03 ppm後排出。由此可見,使用含有濃度3.5重量百分比之氫氧化鈉水溶液吸收二氧化碳確實能有利於降低二氧化碳之排放量。Here, 38.5 kg of carbon dioxide can be absorbed by using 1000 kg of a 3.5 weight percent sodium hydroxide aqueous solution. In an equivalent amount of exhaust gas, the content of carbon dioxide in the treated exhaust gas is reduced from 45 ppm to 0.03 ppm and discharged. It can be seen that the absorption of carbon dioxide by using an aqueous sodium hydroxide solution containing a concentration of 3.5% by weight can indeed help reduce carbon dioxide emissions.

接著,收集該吸收飽和二氧化碳的1000公斤的碳酸氫鈉水溶液,並將其加入含有8500公斤微藻之微藻養殖槽中,供應微藻進行光合作用,藉以降低碳酸氫鈉水溶液中碳酸根離子及碳酸氫根離子的濃度,並得到一經處理的廢水。Next, the 1000 kg sodium bicarbonate aqueous solution that absorbed saturated carbon dioxide was collected and added to a microalga cultivation tank containing 8500 kg of microalgae, and the microalgae were supplied for photosynthesis, thereby reducing the carbonate ion and Concentration of bicarbonate ions and get a treated wastewater.

之後,將經處理的廢水經由過濾、沉澱處理後可得到上清液與含有微藻之藻泥沉澱物;該上清液含有氫氧根離子與鈉離子,可再次回收並導入二氧化碳吸收設備中以吸收廢氣中的二氧化碳;而藻泥沉澱物經由乾燥處理後得到乾藻粉,乾藻粉可直接應用為食品、飼料、肥料之原料或直接當成燃料使用,所述乾藻粉可再利用破壁處理後,取得一藻油及一藻塊,該藻塊可作為動物飼料或肥料;將該藻油進行轉酯處理,可得到生質柴油。After the treated wastewater is filtered and precipitated, a supernatant liquid and algae slurry containing microalgae can be obtained; the supernatant liquid contains hydroxide ions and sodium ions, which can be recovered and introduced into the carbon dioxide absorption equipment again. To absorb carbon dioxide in the exhaust gas; and the algae mud sediment is dried to obtain dried algae powder. The dried algae powder can be directly used as a raw material for food, feed, fertilizer or directly used as a fuel. The dried algae powder can be reused and broken. After the wall treatment, an algae oil and an algae block are obtained, and the algae block can be used as animal feed or fertilizer; the algae oil can be transesterified to obtain biodiesel.

於具體實施方式中,微藻養殖槽係採用全自動密閉式微藻養殖槽,該全自動密閉式微藻養殖槽另設置有酸鹼值偵測器、水流速度偵測器、溫度偵測器、藻密度偵測器及光照度偵測器,其可以自動偵測該微藻養殖槽之水溶液的酸鹼值,當酸鹼值超過8,會自動調節補入碳酸氫鈉水溶液,以維持微藻行光合作用之效率,並且微藻於全自動密閉式微藻養殖槽,相較於開放式微藻養殖槽的產能較高,亦較不受天候變化影響。In a specific embodiment, the microalgae cultivation tank is a fully-automatic closed microalgae cultivation tank, and the fully-automatic closed microalgae cultivation tank is further provided with an acid-base value detector, a water flow speed detector, a temperature detector, and algae. Density detector and illuminance detector, which can automatically detect the pH value of the aqueous solution of the microalgae cultivation tank. When the pH value exceeds 8, the sodium bicarbonate solution will be automatically adjusted to maintain the photosynthesis of the microalgae. The efficiency of the effect, and the microalgae in the fully-automatic closed microalgae cultivation tank, compared with the open microalgae cultivation tank, the production capacity is higher, and it is less affected by weather changes.

本發明之處理方法以鹼性水溶液吸收二氧化碳,有效改善淡水或海水吸收廢氣中二氧化碳溶解度效果不彰的問題;並將所得之弱酸性水溶液加入微藻養殖槽中進行光合作用,解決了碳酸水直接排放而造成環境污染的問題。不僅如此,本發明之處理方法所得到經光合作用反應後的廢水,經過濾沉澱後,上清液可再次回收循環利用,而藻泥經過濾沉澱乾燥而得之乾藻粉更可進一步作為環保能源原料。The treatment method of the present invention absorbs carbon dioxide with an alkaline aqueous solution, which effectively improves the problem of poor solubility of carbon dioxide in the exhaust gas from freshwater or seawater. The obtained weakly acidic aqueous solution is added to a microalga cultivation tank for photosynthesis, which solves the problem of carbonated water directly. The problem of environmental pollution caused by emissions. Not only that, after the photosynthetic reaction wastewater obtained by the treatment method of the present invention is filtered and precipitated, the supernatant can be recycled and reused, and the dried algae powder obtained by filtering and drying the algal slurry can further be used as environmental protection. Energy raw materials.

以上所述僅是為方便說明本發明之一較佳實施例,並非用於限定本發明之範圍,本發明所主張之權利範圍自應以申請專利範圍所述為主。The above description is only for the convenience of describing a preferred embodiment of the present invention, and is not intended to limit the scope of the present invention. The scope of the claimed rights of the present invention should mainly be described in the scope of patent application.

no

圖1為本發明降低二氧化碳排放量之處理方法的流程示意圖。FIG. 1 is a schematic flowchart of a treatment method for reducing carbon dioxide emissions according to the present invention.

no

Claims (17)

一種降低二氧化碳排放量之處理方法,其包含以下步驟: 收集含有二氧化碳之廢氣; 以濃度低於20重量百分比之一鹼性水溶液吸收所述廢氣中的二氧化碳,並得一弱酸性水溶液,所述弱酸性水溶液中含有碳酸根離子、碳酸氫根離子與金屬離子;以及 將該弱酸性水溶液加入含有微藻之微藻養殖槽中進行光合作用,藉以降低弱酸性水溶液中碳酸根離子及碳酸氫根離子的濃度,以得到一經處理的廢水。A treatment method for reducing carbon dioxide emissions, comprising the following steps: collecting exhaust gas containing carbon dioxide; absorbing carbon dioxide in the exhaust gas with an alkaline aqueous solution having a concentration of less than 20% by weight, and obtaining a weakly acidic aqueous solution, the weak The acidic aqueous solution contains carbonate ions, bicarbonate ions, and metal ions; and the weakly acidic aqueous solution is added to a microalgae culture tank containing microalgae for photosynthesis, thereby reducing the carbonate and bicarbonate ions in the weakly acidic aqueous solution. Concentration to get a treated wastewater. 如請求項1所述之處理方法,其中於前述收集含有二氧化碳之廢氣之步驟以及以濃度低於20重量百分比之鹼性水溶液吸收所述廢氣中的二氧化碳並得該弱酸性水溶液之步驟包括: 收集含有二氧化碳之廢氣; 對所述含有二氧化碳之廢氣進行前處理,獲得一經前處理之廢氣,該經前處理之廢氣含有二氧化碳; 以濃度低於20重量百分比之該鹼性水溶液吸收該經前處理之廢氣中的二氧化碳,得到該弱酸性水溶液; 其中,所述前處理為集塵處理、脫硫處理、脫硝處理、降溫處理或其組合。The processing method according to claim 1, wherein the step of collecting the exhaust gas containing carbon dioxide and the step of absorbing the carbon dioxide in the exhaust gas with an alkaline aqueous solution having a concentration of less than 20% by weight to obtain the weakly acidic aqueous solution include: collecting Carbon dioxide-containing exhaust gas; pre-treating the carbon dioxide-containing exhaust gas to obtain a pre-treated exhaust gas, the pre-treated exhaust gas containing carbon dioxide; absorbing the pre-treated exhaust gas with the alkaline aqueous solution having a concentration of less than 20% by weight Carbon dioxide in the exhaust gas to obtain the weakly acidic aqueous solution; wherein the pretreatment is a dust collection treatment, a desulfurization treatment, a denitration treatment, a temperature reduction treatment, or a combination thereof. 如請求項1所述之處理方法,其中該鹼性水溶液為含有IA族元素金屬離子的水溶液、含有IIA族元素金屬離子的水溶液或其組合。The processing method according to claim 1, wherein the alkaline aqueous solution is an aqueous solution containing a group IA element metal ion, an aqueous solution containing a group IIA element metal ion, or a combination thereof. 如請求項3所述之處理方法,其中該鹼性水溶液為氫氧化鈉水溶液、氫氧化鈣水溶液、氫氧化鉀水溶液、氨水溶液或其組合。The method according to claim 3, wherein the alkaline aqueous solution is an aqueous sodium hydroxide solution, an aqueous calcium hydroxide solution, an aqueous potassium hydroxide solution, an aqueous ammonia solution, or a combination thereof. 如請求項4所述之處理方法,其中該鹼性水溶液為氫氧化鈉水溶液。The method according to claim 4, wherein the alkaline aqueous solution is an aqueous sodium hydroxide solution. 如請求項1所述之處理方法,其中該鹼性水溶液之濃度係低於或等於10重量百分比。The method according to claim 1, wherein the concentration of the alkaline aqueous solution is less than or equal to 10 weight percent. 如請求項6所述之處理方法,其中該鹼性水溶液之濃度係高於或等於3重量百分比且低於或等於5重量百分比。The processing method according to claim 6, wherein the concentration of the alkaline aqueous solution is higher than or equal to 3 weight percent and lower than or equal to 5 weight percent. 如請求項1所述之處理方法,其中該弱酸性水溶液之酸鹼值係大於或等於5且小於或等於7。The method according to claim 1, wherein the weakly acidic aqueous solution has a pH value of 5 or more and 7 or less. 如請求項8所述之處理方法,其中該弱酸性水溶液之酸鹼值係大於或等於5且小於或等於6。The processing method according to claim 8, wherein the weakly acidic aqueous solution has a pH value of 5 or more and 6 or less. 如請求項1所述之處理方法,其中該微藻為葡萄藻、小球藻、隱甲藻、細柱藻、杜氏藻、等鞭金藻、單腸藻、微小綠藻、擬球藻、新綠藻、菱形藻、三角褐指藻、裂殖壺菌、司西扁藻或其組合。The processing method according to claim 1, wherein the microalgae are phytoplankton, chlorella, dinoflagellum, cylindrum, Dunaliella, isochrysis, monoenteric algae, micro green algae, pseudococcus, Neo-green algae, diamond-shaped algae, Phaeodactylum tricornutum, Schizochytrium spp., Schizochytrium or a combination thereof. 如請求項1所述之處理方法,其中該微藻養殖槽係一密閉式微藻養殖槽。The processing method according to claim 1, wherein the microalgae cultivation tank is a closed microalgae cultivation tank. 如請求項1所述之處理方法,其中於前述將該弱酸性水溶液加入含有微藻之微藻養殖槽中進行光合作用,藉以降低弱酸性水溶液中碳酸根及碳酸氫根離子的濃度,以得到該經處理的廢水之步驟包括: 將該弱酸性水溶液加入含有微藻之微藻養殖槽中進行光合作用,藉以降低弱酸性水溶液中碳酸根離子及碳酸氫根離子的濃度,獲得一第一處理溶液,該第一處理溶液之酸鹼值大於8; 於該第一處理溶液中補入該弱酸性水溶液,獲得一第二處理溶液,該第二處理溶液之酸鹼值係大於或等於6且小於或等於7,所述第二處理溶液中含有離子、碳酸氫根離子與金屬離子; 於該含有微藻及該第二處理溶液之微藻養殖槽中,令微藻進行光合作用,藉以降低第二處理溶液中碳酸根離子及碳酸氫根離子的濃度,以得到該經處理的廢水。The processing method according to claim 1, wherein the weakly acidic aqueous solution is added to the microalgae-containing microalgae cultivation tank for photosynthesis, thereby reducing the concentration of carbonate and bicarbonate ions in the weakly acidic aqueous solution to obtain The step of treating the treated wastewater includes: adding the weakly acidic aqueous solution to a microalgae culture tank containing microalgae for photosynthesis, thereby reducing the concentration of carbonate ions and bicarbonate ions in the weakly acidic aqueous solution to obtain a first treatment Solution, the pH value of the first treatment solution is greater than 8; adding the weakly acidic aqueous solution to the first treatment solution to obtain a second treatment solution, the pH value of the second treatment solution is greater than or equal to 6 and Less than or equal to 7, the second treatment solution contains ions, bicarbonate ions, and metal ions; in the microalga cultivation tank containing the microalgae and the second treatment solution, the microalgae performs photosynthesis, thereby reducing The concentration of carbonate ions and bicarbonate ions in the second treatment solution to obtain the treated wastewater. 如請求項12所述之處理方法,其中該微藻養殖槽係一全自動微藻養殖槽。The method according to claim 12, wherein the microalgae cultivation tank is a fully automatic microalgae cultivation tank. 如請求項1所述之處理方法,其中於前述將該弱酸性水溶液加入含有微藻之微藻養殖槽中進行光合作用,藉以降低弱酸性水溶液中碳酸根離子及碳酸氫根離子的濃度,以得到該經處理的廢水之步驟之後包括: 將所述經處理的廢水進行後續處理,獲得一上清液與一含有微藻之藻泥沉澱物,所述上清液中含有氫氧根離子與金屬離子;以及 對所述含有微藻之藻泥沉澱物進行乾燥處理,獲得一乾藻粉; 其中,所述後續處理為沉澱處理、過濾處理或其組合。The treatment method according to claim 1, wherein the weakly acidic aqueous solution is added to the microalgae-containing microalgae culture tank for photosynthesis, thereby reducing the concentration of carbonate ions and bicarbonate ions in the weakly acidic aqueous solution, so as to After the step of obtaining the treated wastewater, the method includes the following steps: obtaining a supernatant and a microalgae-containing algae mud precipitate, wherein the supernatant contains hydroxide ions and Metal ions; and drying the microalgae-containing algae mud sediment to obtain a dried algae powder; wherein the subsequent treatment is a precipitation treatment, a filtration treatment, or a combination thereof. 如請求項14所述之處理方法,其中所述濃度低於20重量百分比之鹼性水溶液為所述經處理的廢水進行後續處理所收集得到之上清液;且於前述以濃度低於20重量百分比之該鹼性水溶液吸收所述廢氣中的二氧化碳,並得該弱酸性水溶液之步驟包括: 以該上清液吸收所述廢氣中的二氧化碳,並得該弱酸性水溶液。The processing method according to claim 14, wherein the alkaline aqueous solution having a concentration of less than 20% by weight is a supernatant collected by subsequent treatment of the treated wastewater; The percentage of the alkaline aqueous solution absorbs carbon dioxide in the exhaust gas, and the step of obtaining the weakly acidic aqueous solution includes: absorbing the carbon dioxide in the exhaust gas with the supernatant, and obtaining the weakly acidic aqueous solution. 如請求項15所述之處理方法,其中該上清液為濃度低於或等於5重量百分比之鹼性水溶液。The method according to claim 15, wherein the supernatant is an alkaline aqueous solution having a concentration of less than or equal to 5 weight percent. 如請求項14所述之處理方法,其中於前述對所述含有微藻之藻泥沉澱物進行乾燥處理,獲得該乾藻粉之步驟之後包括: 將該乾藻粉利用破壁處理,取得一藻油及一藻塊; 將該藻油轉酯處理,得一生質柴油。The processing method according to claim 14, wherein after the aforesaid step of drying the algae mud precipitate containing microalgae to obtain the dried algae powder, the method comprises: using the dried algae powder to break the wall to obtain a Algal oil and an algae block; the algal oil is transesterified to obtain a biodiesel.
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RU2759433C1 (en) * 2020-12-03 2021-11-12 Дмитрий Андреевич Зубрилин Air filtration method and device for its implementation
US11413576B2 (en) 2019-06-12 2022-08-16 Cheng-Jen Lin Method for treating gas
TWI829556B (en) * 2023-03-16 2024-01-11 穩碳永續股份有限公司 Production method of inorganic nutrient source and production system thereof

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US11413576B2 (en) 2019-06-12 2022-08-16 Cheng-Jen Lin Method for treating gas
RU2759433C1 (en) * 2020-12-03 2021-11-12 Дмитрий Андреевич Зубрилин Air filtration method and device for its implementation
WO2022119475A1 (en) * 2020-12-03 2022-06-09 Дмитрий Андреевич ЗУБРИЛИН Air filtration method and device for the implementation thereof
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