TWI496882B - 生成生質柴油之方法 - Google Patents
生成生質柴油之方法 Download PDFInfo
- Publication number
- TWI496882B TWI496882B TW103115367A TW103115367A TWI496882B TW I496882 B TWI496882 B TW I496882B TW 103115367 A TW103115367 A TW 103115367A TW 103115367 A TW103115367 A TW 103115367A TW I496882 B TWI496882 B TW I496882B
- Authority
- TW
- Taiwan
- Prior art keywords
- support
- nanoparticle
- compound
- biodiesel
- alkaline earth
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
- C10L1/026—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only for compression ignition
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J19/12—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electromagnetic waves
- B01J19/121—Coherent waves, e.g. laser beams
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J19/12—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electromagnetic waves
- B01J19/122—Incoherent waves
- B01J19/126—Microwaves
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J19/12—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electromagnetic waves
- B01J19/122—Incoherent waves
- B01J19/129—Radiofrequency
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/02—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the alkali- or alkaline earth metals or beryllium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/40—Catalysts, in general, characterised by their form or physical properties characterised by dimensions, e.g. grain size
- B01J35/45—Nanoparticles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60K—ARRANGEMENT OR MOUNTING OF PROPULSION UNITS OR OF TRANSMISSIONS IN VEHICLES; ARRANGEMENT OR MOUNTING OF PLURAL DIVERSE PRIME-MOVERS IN VEHICLES; AUXILIARY DRIVES FOR VEHICLES; INSTRUMENTATION OR DASHBOARDS FOR VEHICLES; ARRANGEMENTS IN CONNECTION WITH COOLING, AIR INTAKE, GAS EXHAUST OR FUEL SUPPLY OF PROPULSION UNITS IN VEHICLES
- B60K15/00—Arrangement in connection with fuel supply of combustion engines or other fuel consuming energy converters, e.g. fuel cells; Mounting or construction of fuel tanks
- B60K15/03—Fuel tanks
- B60K15/04—Tank inlets
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/03—Preparation of carboxylic acid esters by reacting an ester group with a hydroxy group
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60K—ARRANGEMENT OR MOUNTING OF PROPULSION UNITS OR OF TRANSMISSIONS IN VEHICLES; ARRANGEMENT OR MOUNTING OF PLURAL DIVERSE PRIME-MOVERS IN VEHICLES; AUXILIARY DRIVES FOR VEHICLES; INSTRUMENTATION OR DASHBOARDS FOR VEHICLES; ARRANGEMENTS IN CONNECTION WITH COOLING, AIR INTAKE, GAS EXHAUST OR FUEL SUPPLY OF PROPULSION UNITS IN VEHICLES
- B60K15/00—Arrangement in connection with fuel supply of combustion engines or other fuel consuming energy converters, e.g. fuel cells; Mounting or construction of fuel tanks
- B60K15/03—Fuel tanks
- B60K15/035—Fuel tanks characterised by venting means
- B60K15/03519—Valve arrangements in the vent line
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60K—ARRANGEMENT OR MOUNTING OF PROPULSION UNITS OR OF TRANSMISSIONS IN VEHICLES; ARRANGEMENT OR MOUNTING OF PLURAL DIVERSE PRIME-MOVERS IN VEHICLES; AUXILIARY DRIVES FOR VEHICLES; INSTRUMENTATION OR DASHBOARDS FOR VEHICLES; ARRANGEMENTS IN CONNECTION WITH COOLING, AIR INTAKE, GAS EXHAUST OR FUEL SUPPLY OF PROPULSION UNITS IN VEHICLES
- B60K15/00—Arrangement in connection with fuel supply of combustion engines or other fuel consuming energy converters, e.g. fuel cells; Mounting or construction of fuel tanks
- B60K15/03—Fuel tanks
- B60K2015/03256—Fuel tanks characterised by special valves, the mounting thereof
- B60K2015/03289—Float valves; Floats therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60K—ARRANGEMENT OR MOUNTING OF PROPULSION UNITS OR OF TRANSMISSIONS IN VEHICLES; ARRANGEMENT OR MOUNTING OF PLURAL DIVERSE PRIME-MOVERS IN VEHICLES; AUXILIARY DRIVES FOR VEHICLES; INSTRUMENTATION OR DASHBOARDS FOR VEHICLES; ARRANGEMENTS IN CONNECTION WITH COOLING, AIR INTAKE, GAS EXHAUST OR FUEL SUPPLY OF PROPULSION UNITS IN VEHICLES
- B60K15/00—Arrangement in connection with fuel supply of combustion engines or other fuel consuming energy converters, e.g. fuel cells; Mounting or construction of fuel tanks
- B60K15/03—Fuel tanks
- B60K15/04—Tank inlets
- B60K2015/0458—Details of the tank inlet
- B60K2015/0477—Details of the filler neck tank side
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L2200/00—Components of fuel compositions
- C10L2200/04—Organic compounds
- C10L2200/0461—Fractions defined by their origin
- C10L2200/0469—Renewables or materials of biological origin
- C10L2200/0476—Biodiesel, i.e. defined lower alkyl esters of fatty acids first generation biodiesel
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L2250/00—Structural features of fuel components or fuel compositions, either in solid, liquid or gaseous state
- C10L2250/06—Particle, bubble or droplet size
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L2270/00—Specifically adapted fuels
- C10L2270/02—Specifically adapted fuels for internal combustion engines
- C10L2270/026—Specifically adapted fuels for internal combustion engines for diesel engines, e.g. automobiles, stationary, marine
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/36—Applying radiation such as microwave, IR, UV
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Physics & Mathematics (AREA)
- Toxicology (AREA)
- Electromagnetism (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Combustion & Propulsion (AREA)
- Transportation (AREA)
- Mechanical Engineering (AREA)
- Optics & Photonics (AREA)
- Fats And Perfumes (AREA)
Description
本發明係關於一種生成生質柴油之方法,尤指一種簡單、快速且環保之生成生質柴油之方法。
生質柴油(Biodiesel)是利用動植物油脂或廢食用油之長鏈脂肪酸,於觸媒存在下與烷基醇類反應產生烷基酯類之燃料,已證明為有效的柴油車輛引擎的燃料,可改善引擎排放廢氣的品質,且不需修改既有石化柴油引擎有關設備,可直接使用或做為石化柴油添加劑,其十六烷值比石化柴油為高,閃火點(Flash point)較低,可安全使用;例如:美國環保署(EPA)已認可B100(純生質柴油,如黃豆脂肪酸甲酯)及B20(生質柴油20%與石化柴油80%的混合油)為替代柴油燃料,可減少污染物排放,而改善環境空氣品質。
習知將動植物油或廢食用油轉化成為生質柴油技術,包括稀釋、裂解、微乳化與轉酯化,其中以轉酯化較具效率;廢食用油在轉酯化前需經一前處理,先經過濾器過濾,再以蒸餾的方式將水份去除,而其中游離脂肪酸則以預酯化的方式進行處理,精鍊程序多而繁雜,若品質控制不穩定,則會影響後續生質柴油轉酯化反應之效
率。而在轉酯化反應中,與低碳醇以及鹼觸媒混合,靜置使甲基酯層(粗生質柴油)與甘油層分離,上層粗生質柴油再重複進行轉酯化反應,最後將粗生質柴油進行蒸餾回收甲醇、中和、水洗、及蒸餾去除水分,得到純生質柴油;此程序之單道轉化率低,操作步驟多,操作時間較長,設備費用也較高。
因此,在環保意識抬頭,生質柴油需求越高之情況下,若能將廢食用油以簡單、快速的方式生成生質柴油,對經濟、環保將有很大貢獻。
本發明之主要目的係在提供一種生成生質柴油之方法,俾能以單一步驟簡單快速的生成生質柴油,且無需使用任何強酸鹼性之化學物質,避免對環境造成汙染。
為達成上述目的,本發明提供一種生成生質柴油之方法,包括:提供一奈米粒,包含一化合物,該化合物為一鹼金屬化合物或一鹼土金屬化合物;將該奈米粒附著至一支撐體上,形成一複合物;以及將該複合物與一目標物接觸,進行一轉酯化反應。
其中,該奈米粒包含之化合物可為鹼金屬化合物或鹼土金屬化合物,鹼金屬化合物包括:鋰(Li)、鈉(Na)、鉀(K)、銣(Rb)、銫(Cs)、鍅(Fr)化合物,鹼土金屬化合物包括:鈹(Be)、鎂(Mg)、鈣(Ca)、鍶(Sr)、鋇(Ba)、鐳(Ra)化合物。並且,該化合物較佳為一鹼金屬氧化物或一鹼土金屬氧化物,更佳為鹼土金屬氧化物,例如:氧化鋇(BaO)、氧
化鍶(SrO)、氧化鈣(CaO)或氧化鎂(MgO)。以催化轉酯化反應之催化活性來看,催化活性依序為氧化鋇(BaO)>氧化鍶(SrO)>氧化鈣(CaO)>氧化鎂(MgO),然而,因氧化鍶(SrO)難溶於植物油、甲醇、脂肪酸甲基酯中,應用到本發明之方法中,當反應完成後,可輕易從生質柴油或其他副產物中分離出來;故最佳為使用氧化鍶奈米粒。
該奈米粒之尺寸不受限,例如20nm至1000nm皆可適用,較佳為100nm至500nm,更佳為90nm至200nm;以及以該奈米粒和該支撐體之總重為基準,附著至該支撐體上的該奈米粒可為0.5-10wt%,較佳為2-5wt%;然而,本技術領域中具有通常知識者可依實際使用需求,考量能源提供方式、催化效果或催化表面積等因素而選擇,下述實施例中所使用的條件並非用以限制本發明。
在本發明之方法中,該支撐體並無特別限制,可使用本技術領域中常見之載體,例如二氧化矽或其他矽酸鹽類載體。該支撐體之尺寸亦不受限,本技術領域中具有通常知識者可依實際使用需求(包含催化效果、催化表面積、能源提供方式、及奈米粒尺寸)而選擇適當尺寸,例如1mm至30mm,較佳為1mm至16mm,更佳為1mm至3mm;下述實施例中所使用的條件並非用以限制本發明。
在本發明之方法中,該轉酯化反應可進行一微波處理、一射頻處理(Radio frequency,RF)、或一雷射處理,該微波處理、射頻處理、或雷射處理時之使用功率、及處理時間皆不受限,可由本技術領域中具有通常知識者考量
處理方式的能量強弱、溫度高低、聚焦面積等條件而簡單調整,例如當使用較高能量、較高溫度針對較精準之聚焦面積進行處理時,因較集中施予能量,故處理時間較短;相反地,若使用較低能量、較低溫度針對較廣大之聚焦面積進行處理時,則需耗費較多的時間進行轉酯化反應。或者,在較高精準度之聚焦面積之情況下,亦可採取低功率、低溫加熱的方式進行轉酯化反應,達到節能(低耗能)的效果。具體舉例說明:當使用800W至1200W之微波處理時,處理溫度至少為60℃,處理時間可為10秒至3分鐘;或當使用1000W至1200W,處理溫度為65℃至80℃,處理時間可為10秒至2分鐘。若有需要,該轉酯化反應的處理步驟也可以採取批次進行、或連續進行的方式,僅需達到所需的轉酯化反應程度即可,換言之,無論選擇何種處理進行轉酯化反應,僅需在目標物之預定面積內達到進行轉酯化反應所需的溫度即可。
在本發明之方法中,該奈米粒可不僅是附著至該支撐體上,而該奈米粒之部分較佳可更進一步嵌入該支撐體中,使奈米粒不易從支撐體上剝離。達成該嵌入的方式並無特別限制,例如可藉由較高溫度進行轉酯化反應,將該支撐體軟化,而使該奈米粒之部分嵌入該支撐體中;或者,該奈米粒之部分與該支撐體之間可形成一第二化合物,例如:當氧化鍶奈米粒嵌入二氧化矽顆粒時,氧化鍶奈米粒和二氧化矽顆粒間之界面可能形成穩定的矽酸鍶(SrSiO3
)化合物。顯而易見地,該第二化合物會因奈米粒和
支撐體的種類而有所變化。
此外,目標物的種類並未特別限制,可為任何能夠產生生質柴油的原料,例如大豆(soybean)、棉花籽油、廢食用油、及藻類等;但目標物種類也會影響微波處理的時間,例如:當以1200W的微波處理進行轉酯化反應之情況下,目標物為大豆(soybean)時,反應僅需約40秒;目標物為藻類時,反應僅需約2分鐘;而目標物為廢食用油時,反應需約3分鐘;即可達到油量90%以上皆轉換成生質柴油。
台灣人的飲食習慣,導致每天產生大量廢食用油,利用本發明之方法,回收家庭、餐廳或學校產出的廢油,將其中三酸甘油酯轉換成生質柴油能源,對經濟、環保將有很大貢獻。經奈米粒催化進行轉脂化反應後,可自動分成最上方的生質柴油層、最下方的副產物甘油層及位於兩者中間的氧化鍶催化劑層;催化劑可回收再次使用,而生質柴油及甘油都有經濟價值,轉化過程中沒有浪費任何材料。
和習知的催化劑相比,例如氫氧化鉀(KOH)、氫氧化鈉(NaOH),在反應後會溶解於生質柴油層以及甘油層中,需進行後續分離、純化,且難以回收催化劑。因此,本發明之方法明顯可減少處理程序、降低所需成本以及有效增加最終產物的純度,且催化劑易於分離而可回收再重複利用。此外,本發明之方法不需使用強酸鹼性之化學物質,避免對環境造成汙染,副產物亦具有產業應用性而非
需丟棄之廢棄物。
圖1A係本發明一較佳實施例之奈米粒之掃描式電子顯微鏡(SEM)影像。
圖1B係本發明一較佳實施例之奈米粒之能譜儀(EDS)光譜。
圖2係本發明一較佳實施例之奈米粒之X光繞射分析圖(XRD)。
圖3為係本發明一較佳實施例之奈米粒之動態光散射儀(DLS)分析圖。
圖4係本發明一較佳實施例之生質柴油之核磁共振儀(NMR)圖譜。
圖5A係本發明一較佳實施例之奈米粒之催化能力之穩定性測試結果。
圖5B係本發明一較佳實施例之微藻樣品之油量百分比。
圖6A係本發明另一較佳實施例之生質柴油轉換率結果。
圖6B係本發明再一較佳實施例之生質柴油轉換率結果。
[合成氧化鍶(SrO)奈米粒]
取40ml苯甲醇(benzyl alcohol)於燒杯中,加入0.5克乙醯丙酮鍶(strontium acetyl acetonate),再加入1.5克粒徑約1mm的二氧化矽顆粒。將該混合物置於1200W
的微波爐中加熱10分鐘。上述反應係在氬氣環境中進行,防止二氧化碳分子影響而生成碳酸鍶(SrCO3
)。反應完成後,氧化鍶奈米粒附著在二氧化矽顆粒上,圖1A所示為其之掃描式電子顯微鏡(SEM)影像,可看出氧化鍶奈米粒緊密包覆於整個二氧化矽顆粒表面,以氧化鍶奈米粒和二氧化矽顆粒之總重為基準,約有2-5wt%氧化鍶奈米粒附著在二氧化矽顆粒上面,氧化鍶奈米粒的尺寸約為100nm;另圖1B為其之能譜儀(EDS)光譜。在圖1B中,可以觀察到該產物包含鍶(Sr)和氧(O),而偵測到碳(C)的存在係因少量二氧化碳分子參與反應而生成碳酸鍶(SrCO3
)。
圖2為附著在二氧化矽顆粒上之氧化鍶奈米粒之X光繞射分析圖(XRD),(a)組表示於700℃下加熱之產物,(b)組表示於800℃下加熱之產物。圖2的結果表示:於700℃下加熱,產物中的主成分為碳酸鍶(SrCO3
);而經於800℃下加熱,得到氧化鍶(SrO)產物。因此,加熱溫度較佳為800℃以上(較佳為850℃以上),比較不容易生成碳酸鍶(SrCO3
)。
圖3為該產物之動態光散射儀(DLS)分析圖。圖3結果顯示氧化鍶(SrO)奈米粒的尺寸分布,其平均粒徑為136nm。據此,動態光散射儀(DLS)分析的粒徑結果符合掃描式電子顯微鏡(SEM)影像下計算的粒徑。
[轉酯化反應-微藻]
利用上述製備的附著在二氧化矽顆粒上的氧化鍶奈米粒,對擬球藻(Nannochloropsis microalgae)進行轉
酯化反應,測試其催化效果,該轉酯化反應係在1200W的微波爐中直接以乾燥樣品進行,而不須先進行脂量(lipidic mass)萃取。在微波爐中進行轉酯化的時間為2分鐘,生成脂肪酸甲基酯(FAME)產物(即為生質柴油);將其溶於氯化鎘(CDCl3
)中,以200-MHz1
H核磁共振儀(NMR)測量生質柴油的轉換率,並對波峰下的面積積分,計算出樣品中油(oil)比生質柴油的轉換百分比。
圖4係本發明一較佳實施例之生質柴油之核磁共振儀(NMR)圖譜。在圖4中,於44~35ppm範圍內不存在三酸甘油酯的波峰,並且在3.65ppm偵測到甲基酯中的甲基波峰。因此,圖4之結果顯示甲基的單一波峰訊號強,且生成的生質柴油中已完全不含三酸甘油酯。
由上述結果,經過2分鐘反應後,三酸甘油酯完全轉換成生質柴油,計算出轉換率高達99.9%,且微藻中的油量為37%。
另外,使用市售的微米級氧化鍶(SrO,Sigma-Aldrich)進行轉酯化反應,實驗條件皆與上述相同,但在微波爐中進行轉酯化的時間需耗費5分鐘,為氧化鍶奈米粒的2.5倍。
為了測試重複使用的催化效果,利用氧化鍶奈米粒進行轉酯化反應後,將氧化鍶奈米粒與擬球藻分離,置入甲醇形成新的混合物後,再對新的微藻樣品進行轉酯,每次反應都進行2分鐘。測試結果如圖5A所示,證實氧化鍶奈米粒的催化穩定性,可維持一定的轉換率,第一
次反應至第六次反應的生質柴油轉換率為99.9至97.9%。
由於無法將擬球藻從氧化鍶奈米粒表面完全移除,第一次反應的油量為37%,到第六次反應時油量升高至41.3%,如圖5B所示。
[轉酯化反應-廢棄用油]
利用上述製備的氧化鍶奈米粒催化廢棄用油(收集自佳駒公司,酸值(KOH)約為2.0)。混合15克廢棄用油、甲醇、及氧化鍶奈米粒,經磁石混合器攪拌均勻,在1000W的微波爐中進行轉酯化反應,分別測試進行轉酯化的時間:1、2、3、4、5及6分鐘,利用分析設備(GC-FID HP 6890),以ASTM D6751及EN14214分析方法,計算生質柴油(脂肪酸甲基酯(FAME))的轉換率,其結果如圖6A所示。請參照圖6A,當在微波反應時間為3分鐘時,可達到最佳的廢食用油轉酯化效果,生質柴油轉換率約為92%,酸值(KOH)約為0.4,消耗電量約0.081kW,生成甘油副產物約10%。
另外,除了在700W的微波爐中進行轉酯化反應,以相同的實驗條件測試氧化鍶奈米粒催化廢棄用油,其結果如圖6B所示,微波反應時間為6分鐘時,可達到最佳的廢食用油轉酯化效果。
上述實施例僅係為了方便說明而舉例而已,本發明所主張之權利範圍自應以申請專利範圍所述為準,而非僅限於上述實施例。
Claims (14)
- 一種生成生質柴油之方法,包括:提供一奈米粒,包含一化合物,該化合物為一鹼金屬化合物或一鹼土金屬化合物;將該奈米粒附著至一支撐體上,形成一複合物;以及將該複合物與一目標物接觸,進行一轉酯化反應。
- 如申請專利範圍第1項所述之方法,其中,該化合物為一鹼金屬氧化物或一鹼土金屬氧化物。
- 如申請專利範圍第2項所述之方法,其中,該鹼土金屬氧化物為氧化鋇(BaO)、氧化鍶(SrO)、氧化鈣(CaO)或氧化鎂(MgO)。
- 如申請專利範圍第3項所述之方法,其中,該鹼土金屬氧化物為氧化鍶(SrO)。
- 如申請專利範圍第1項所述之方法,其中,該支撐體為一矽酸鹽類載體。
- 如申請專利範圍第5項所述之方法,其中,該支撐體為一二氧化矽載體。
- 如申請專利範圍第1項所述之方法,其中,將該奈米粒之一部分嵌入該支撐體。
- 如申請專利範圍第7項所述之方法,其中,該奈米粒之該部分與該支撐體之間係形成一第二化合物。
- 如申請專利範圍第1項所述之方法,其中,該支撐體之尺寸為1mm至30mm。
- 如申請專利範圍第1項所述之方法,其中,該奈米粒之尺寸為20nm至1000nm。
- 如申請專利範圍第1項所述之方法,其中,以該奈米粒和該支撐體之總重為基準,附著至該支撐體上的該奈米粒為0.5至10wt%。
- 如申請專利範圍第1項所述之方法,其中,該轉酯化反應係進行一微波處理、一射頻處理(Radio frequency,RF)、或一雷射處理。
- 如申請專利範圍第12項所述之方法,其中,該微波處理時之溫度至少為60℃。
- 如申請專利範圍第1項所述之方法,其中,該目標物係選自由:大豆(soybean)、棉花籽油、廢食用油、及藻類所組成之群組。
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US201361921172P | 2013-12-27 | 2013-12-27 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| TW201525128A TW201525128A (zh) | 2015-07-01 |
| TWI496882B true TWI496882B (zh) | 2015-08-21 |
Family
ID=53481032
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| TW103115367A TWI496882B (zh) | 2013-12-27 | 2014-04-29 | 生成生質柴油之方法 |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US20150184096A1 (zh) |
| TW (1) | TWI496882B (zh) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI582225B (zh) * | 2015-10-19 | 2017-05-11 | 張志雄 | 廢食用油快速裂解產製低酸值生質汽柴油的製程 |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105602632A (zh) * | 2016-01-06 | 2016-05-25 | 山东泰德新能源有限公司 | 一种生物柴油制备方法 |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7790651B2 (en) * | 2006-07-23 | 2010-09-07 | Iowa State University Research Foundation, Inc. | Porous silica and metal oxide composite-based catalysts for conversion of fatty acids and oils to biodiesel |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20090005582A1 (en) * | 2007-06-22 | 2009-01-01 | Greg Anderson | Vessels and methods for synthesis of biofuel |
| US8507702B2 (en) * | 2011-03-29 | 2013-08-13 | Southwest Research Institute | Continuous production of bioderived esters via supercritical solvent processing using solid heterogeneous catalysts |
-
2014
- 2014-04-29 TW TW103115367A patent/TWI496882B/zh not_active IP Right Cessation
- 2014-10-29 US US14/526,736 patent/US20150184096A1/en not_active Abandoned
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7790651B2 (en) * | 2006-07-23 | 2010-09-07 | Iowa State University Research Foundation, Inc. | Porous silica and metal oxide composite-based catalysts for conversion of fatty acids and oils to biodiesel |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI582225B (zh) * | 2015-10-19 | 2017-05-11 | 張志雄 | 廢食用油快速裂解產製低酸值生質汽柴油的製程 |
Also Published As
| Publication number | Publication date |
|---|---|
| US20150184096A1 (en) | 2015-07-02 |
| TW201525128A (zh) | 2015-07-01 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Dai et al. | One-pot synthesis of acid-base bifunctional catalysts for biodiesel production | |
| Narasimhan et al. | Heterogeneous nanocatalysts for sustainable biodiesel production: A review | |
| Pandit et al. | Biodiesel production from microalgal biomass using CaO catalyst synthesized from natural waste material | |
| Roschat et al. | Rubber seed oil as potential non-edible feedstock for biodiesel production using heterogeneous catalyst in Thailand | |
| Sharma et al. | Exploration of upstream and downstream process for microwave assisted sustainable biodiesel production from microalgae Chlorella vulgaris | |
| Syazwani et al. | Low-cost solid catalyst derived from waste Cyrtopleura costata (Angel Wing Shell) for biodiesel production using microalgae oil | |
| BODDULA | Microwaves in organic synthesis | |
| Patil et al. | Comparison of direct transesterification of algal biomass under supercritical methanol and microwave irradiation conditions | |
| Mumtaz et al. | Biodiesel production through chemical and biochemical transesterification: Trends, technicalities, and future perspectives | |
| Lam et al. | Catalytic transesterification of high viscosity crude microalgae lipid to biodiesel: Effect of co-solvent | |
| Santiago-Torres et al. | Sodium zirconate (Na2ZrO3) as a catalyst in a soybean oil transesterification reaction for biodiesel production | |
| Sharma et al. | An ideal feedstock, kusum (Schleichera triguga) for preparation of biodiesel: Optimization of parameters | |
| Kumar et al. | Nanocrystalline lithium ion impregnated calcium oxide as heterogeneous catalyst for transesterification of high moisture containing cotton seed oil | |
| ES2662743T3 (es) | Proceso para preparar biodiésel con lipasa y deshidratación en línea separada | |
| Qing et al. | Reaction kinetics of biodiesel synthesis from waste oil using a carbon-based solid acid catalyst | |
| Sanjay | Heterogeneous catalyst derived from natural resources for biodiesel production: A review | |
| Xiang et al. | A quick method for producing biodiesel from soy sauce residue under supercritical carbon dioxide | |
| Liu et al. | Euonymus maackii Rupr. Seed oil as a new potential non-edible feedstock for biodiesel | |
| Teo et al. | Biodiesel synthesis from photoautotrophic cultivated oleoginous microalgae using a sand dollar catalyst | |
| Zamberi et al. | Biodiesel production from high FFA rubber seed oil using waste cockles | |
| CN102199493A (zh) | 固体碱催化作用下生物柴油的一种绿色制备方法 | |
| Yameen et al. | Biodiesel production from marine macroalgae Ulva lactuca lipids using novel Cu-BTC@ AC catalyst: Parametric analysis and optimization | |
| Zamberi et al. | Heterogeneous transesterification of rubber seed oil biodiesel production | |
| KR102499622B1 (ko) | 바이오디젤 제조용 고체 산 촉매, 바이오디젤 제조용 고체 염기 촉매, 이들의 제조 방법, 및 이들을 이용한 바이오디젤의 제조 방법 | |
| TWI496882B (zh) | 生成生質柴油之方法 |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| MM4A | Annulment or lapse of patent due to non-payment of fees |