TWI421229B - Environmental friendly process of sensitizers for dye sensitized solar cells - Google Patents

Environmental friendly process of sensitizers for dye sensitized solar cells Download PDF

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TWI421229B
TWI421229B TW99128607A TW99128607A TWI421229B TW I421229 B TWI421229 B TW I421229B TW 99128607 A TW99128607 A TW 99128607A TW 99128607 A TW99128607 A TW 99128607A TW I421229 B TWI421229 B TW I421229B
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bipyridine
dicarboxylic acid
solution
purity
acid
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TW201209015A (en
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Yu Chou Chao
Yu Ting Chang
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Univ Nat Taipei Technology
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染料敏化太陽能電池敏化劑之環保製程Environmentally friendly process for dye-sensitized solar cell sensitizer

本發明係關於染料敏化太陽能電池之敏化染料之純化。特定言之,本發明提供一種純化4,4'-二羧酸-2,2'-聯吡啶(4,4'-dicarboxy-2,2'-bipyridine)的方法。The present invention relates to the purification of sensitizing dyes for dye-sensitized solar cells. In particular, the present invention provides a process for purifying 4,4'-dicarboxy-2,2'-bipyridine.

染料敏化太陽能電池主要是模仿光合作用原理而研製出來的一種新型太陽能電池,其主要優點為原材料豐富、成本低、製造技術相對簡單、在大規模工業化生產中具有較大的優勢,同時所有原材料和製造技術均為無毒、無污染,且部分材料可以充分回收,對保護人類環境具有重要的意義。綜言之,相較於傳統的太陽能電池,染料敏化太陽能電池染料敏化太陽能電池具有下列優點:(1)使用壽命可長達15-20年;(2)結構簡單、易於製造且生產技術簡單,易於大規模工業化生產;(3)生產成本較低,僅為矽太陽能電池的1/5~1/10;(4)製造過程耗費能源較少;(5)製造過程無毒且無污染。The dye-sensitized solar cell is mainly a new type of solar cell developed by imitating the principle of photosynthesis. Its main advantages are abundant raw materials, low cost, relatively simple manufacturing technology, and great advantages in large-scale industrial production, and all raw materials. And manufacturing technology is non-toxic, non-polluting, and some materials can be fully recovered, which is of great significance for the protection of the human environment. In summary, dye-sensitized solar cell dye-sensitized solar cells have the following advantages compared to conventional solar cells: (1) the service life can be as long as 15-20 years; (2) the structure is simple, easy to manufacture and production technology Simple, easy to large-scale industrial production; (3) low production cost, only 1/5 to 1/10 of solar cells; (4) less energy consumption in the manufacturing process; (5) non-toxic and non-polluting in the manufacturing process.

染料敏化太陽能電池主要由奈米多孔半導體薄膜、染料敏化劑、氧化還原電解質、對電極和導電基底等部分組成。奈米多孔半導體薄膜通常為金屬氧化物(TiO2 、SnO2 、ZnO等),聚集在有透明導電膜的玻璃板上作為染料敏化太陽能電池的負極,對電極作為還原催化劑,通常在帶有透明導電膜的玻璃上鍍上鉑。敏化染料吸附在奈米多孔二氧化鈦膜面上,正負極間填充的是含有氧化還原電對的電解質。The dye-sensitized solar cell is mainly composed of a nanoporous semiconductor film, a dye sensitizer, a redox electrolyte, a counter electrode, and a conductive substrate. The nanoporous semiconductor thin film is usually a metal oxide (TiO 2 , SnO 2 , ZnO, etc.), which is collected on a glass plate having a transparent conductive film as a negative electrode of a dye-sensitized solar cell, and the counter electrode is used as a reduction catalyst, usually with The glass of the transparent conductive film is plated with platinum. The sensitizing dye is adsorbed on the surface of the nanoporous titanium dioxide film, and the electrolyte containing the redox couple is filled between the positive and negative electrodes.

應用於染料敏化太陽電池之染料敏化劑可分為兩大類:金屬錯合物色素類,包括釕系列色素類及其他金屬系列色素類(如Os,Fe,Cu,Pt),及有機色素類,包括甲基染料色素類及其他有機色素類(如酞菁,偶氮,香豆素)。目前在染料敏化太陽能電池領域內,以釕金屬為主的系列染料為主流。US20050139257A1提供一種具通式MLX2之光敏化過渡金屬複合物,其中M為選自Ru(II)、Os(II)、Fe(II)、Re(I)及Tc(I)的過渡金屬;L為聚吡啶配體;及X為選自NCS- 、Cl- 、Br- 、I- 、CN- 、NCO- 、H2 O及吡啶基組成之基團的配體。US7321037揭露一種應用於染料敏化太陽電池之含釕複合物的光敏化染劑。Dye sensitizers for dye-sensitized solar cells can be divided into two categories: metal complex pigments, including bismuth series pigments and other metal series pigments (such as Os, Fe, Cu, Pt), and organic pigments. Classes, including methyl dyes and other organic pigments (such as phthalocyanine, azo, coumarin). At present, in the field of dye-sensitized solar cells, a series of dyes based on base metals are the mainstream. US20050139257A1 provides a photosensitized transition metal complex of the formula MLX2 wherein M is a transition metal selected from the group consisting of Ru(II), Os(II), Fe(II), Re(I) and Tc(I); ligand groups, H 2 O and consisting of pyridyl - and X is selected from NCS -, Cl -, Br - , I -, CN -, NCO; polypyridine ligands. US7321037 discloses a photosensitizing dye for a cerium-containing composite applied to a dye-sensitized solar cell.

製備光敏化染料(例如N3,Z907,N719,N854,K8,K19,K73,Z910,Z955)的關鍵原料4,4'-二羧酸-2,2'-聯吡啶(4,4'-dicarboxy-2,2'-bipyridine)為非常重要的配位基,其主要功用在於使染料與TiO2 產生鍵結。此一配位基費用相當昂貴,目前大多自行合成為主。然而,合成出來的粗產物須進一步純化始能做為染料敏化太陽能電池敏化劑之原料。習知技術對於4,4'-二羧酸-2,2'-聯吡啶之純化需使用50%之硝酸沸騰四個小時(Adremi R. Oki and Robert J. Morgan,Syn. Comm.,1995,25(24),4093-4097;Martin Lang,Susanne Lang-Fugmann,and Wolfgang Steglich,org. Syn.,2004,10,432)。但經過此純化過程後之產物純度仍不理想,且過程中所產生之廢酸液污染嚴重,處理費用昂貴不具市場競爭力,也連帶影響染料敏化太陽能電池之經濟效益。綜言之,上述硝酸沸騰純化法具有下列缺點:4,4'-dicarboxylic acid-2,2'-bipyridine (4,4'-dicarboxy), a key material for the preparation of photosensitizing dyes (eg N3, Z907, N719, N854, K8, K19, K73, Z910, Z955) -2,2'-bipyridine) is a very important ligand whose main function is to bond the dye to TiO 2 . This kind of ligand base is quite expensive, and most of them are mainly self-synthesis. However, the crude product synthesized must be further purified to be a raw material for the dye-sensitized solar cell sensitizer. Conventional techniques for the purification of 4,4'-dicarboxylic acid-2,2'-bipyridine require boiling with 50% nitric acid for four hours (Adremi R. Oki and Robert J. Morgan, Syn. Comm., 1995, 25(24), 4093-4097; Martin Lang, Susanne Lang-Fugmann, and Wolfgang Steglich, org. Syn., 2004, 10, 432). However, the purity of the product after the purification process is still not satisfactory, and the waste acid liquid generated in the process is seriously polluted, and the treatment cost is not competitive in the market, and the economic benefit of the dye-sensitized solar cell is also affected. In summary, the above-mentioned nitric acid boiling purification method has the following disadvantages:

(1) 硝酸是一種具揮發性的強酸,在工業生產中對鍋爐具有強腐蝕性,且會釋放出有毒的NO2 氣體。(1) Nitric acid is a volatile, strong acid that is highly corrosive to boilers in industrial production and releases toxic NO 2 gas.

(2) 硝酸在沸騰狀態下有產生爆炸的危險性。(2) Nitric acid has a risk of explosion in boiling state.

(3) 此方法過程中需加熱至沸騰4個小時,增加能源的消耗。(3) This method needs to be heated to boiling for 4 hours to increase energy consumption.

(4) 利用此純化方法產生之廢水為強酸性,對於環境會造成的嚴重污染。(4) The wastewater produced by this purification method is strongly acidic and causes serious pollution to the environment.

(5) 即使經過此法純化一次,產物純度仍不理想,需再重複一次純化過程。(5) Even after purification by this method, the purity of the product is not satisfactory, and the purification process needs to be repeated one more time.

因此,本技藝中仍需要一種更安全、便宜、污染低及純度提高的4,4'-二羧酸-2,2'-聯吡啶之純化方法。Therefore, there is still a need in the art for a method for purifying 4,4'-dicarboxylic acid-2,2'-bipyridine which is safer, less expensive, less polluting and of increased purity.

本發明利用鹼性溶液及酸性溶液處理4,4'-二羧酸-2,2'-聯吡啶而得到純度提高的4,4'-二羧酸-2,2'-聯吡啶。本發明純化方法較習知技術更安全、污染性、更便宜且得到純度更高的產物。本發明純化方法使用較便宜的鹼及酸性溶液處理不純之4,4'-二羧酸-2,2'-聯吡啶,且在室溫下即可進行,與習知技術之方法相比,較為方便、安全、便宜,且產生之廢水pH值呈中性,不僅符合排放標準,更具有廢水再利用之優點。The invention utilizes an alkaline solution and an acidic solution to treat 4,4'-dicarboxylic acid-2,2'-bipyridine to obtain 4,4'-dicarboxylic acid-2,2'-bipyridine having improved purity. The purification process of the present invention is safer, more polluting, less expensive, and yields a higher purity product than conventional techniques. The purification method of the present invention processes the impure 4,4'-dicarboxylic acid-2,2'-bipyridine using a relatively inexpensive alkali and an acidic solution, and can be carried out at room temperature, compared with the method of the prior art. It is more convenient, safe and cheap, and the pH value of the produced wastewater is neutral, which not only meets the emission standards, but also has the advantages of wastewater reuse.

本發明提供一種純化4,4'-二羧酸-2,2'-聯吡啶之方法,其包括下列步驟:The invention provides a method for purifying 4,4'-dicarboxylic acid-2,2'-bipyridine, which comprises the following steps:

(a) 使用鹼性溶液將不純之4,4'-二羧酸-2,2'-聯吡啶攪拌溶解;(a) stirring and dissolving the impure 4,4'-dicarboxylic acid-2,2'-bipyridine using an alkaline solution;

(b) 將酸性溶液以滴定之方式加入所得混合液中,得到析出之產物,即純化之4,4'-二羧酸-2,2'-聯吡啶;及(b) adding an acidic solution to the resulting mixture by titration to obtain a precipitated product, ie, purified 4,4'-dicarboxylic acid-2,2'-bipyridine;

(c) 過濾懸浮液並將過濾物與析出之產物合併,乾燥後即可得到高純度之4,4'-二羧酸-2,2'-聯吡啶。(c) The suspension is filtered and the filtrate is combined with the precipitated product to obtain a high purity 4,4'-dicarboxylic acid-2,2'-bipyridine.

根據本發明,步驟(a)中之鹼性溶液可為鹼金族氫氧化物溶液或氨水。較佳地,該鹼性溶液為鹼金族氫氧化物或氨水;更佳地,該鹼性溶液為氫氧化鈉、氫氧化鉀、氫氧化鋰或氨水。最佳地,該鹼性溶液為氫氧化鈉溶液。According to the invention, the alkaline solution in step (a) may be an alkali gold hydroxide solution or aqueous ammonia. Preferably, the alkaline solution is an alkali gold hydroxide or ammonia water; more preferably, the alkaline solution is sodium hydroxide, potassium hydroxide, lithium hydroxide or ammonia water. Most preferably, the alkaline solution is a sodium hydroxide solution.

根據本發明,步驟(b)中之酸性溶液可為任何酸性溶液。較佳地,該酸性溶液為鹽酸、硝酸、硫酸及醋酸。更佳地,該酸性溶液為鹽酸。經步驟(b)中之酸性溶液處理析出後的產物為純化的4,4'-二羧酸-2,2'-聯吡啶。According to the invention, the acidic solution in step (b) can be any acidic solution. Preferably, the acidic solution is hydrochloric acid, nitric acid, sulfuric acid and acetic acid. More preferably, the acidic solution is hydrochloric acid. The product precipitated by the acidic solution in the step (b) is purified 4,4'-dicarboxylic acid-2,2'-bipyridine.

根據本發明,步驟(a)中之鹼性溶液及步驟中(b)之酸性溶液可為任何濃度。根據本發明,步驟(a)中之鹼性溶液及步驟(b)中之酸性溶液的濃度可根據使用的鹼種類及酸種類調配濃度使得經過之酸性溶液滴定步驟後之溶液之pH值為中性。該溶液為中性廢液,符合排放標準,不會對環境造成污染,更具有廢水再利用之優點。較佳地,步驟中(b)之酸性溶液的濃度至少與步驟(a)中之鹼性溶液的濃度相同。更佳地,步驟中(b)之酸性溶液的濃度大於步驟(a)中之鹼性溶液的濃度。According to the present invention, the alkaline solution in the step (a) and the acidic solution in the step (b) may be in any concentration. According to the present invention, the concentration of the alkaline solution in the step (a) and the acidic solution in the step (b) may be adjusted according to the type of the base to be used and the acid type, so that the pH of the solution after the acidic solution titration step is medium. Sex. The solution is a neutral waste liquid, meets emission standards, does not pollute the environment, and has the advantages of wastewater reuse. Preferably, the concentration of the acidic solution in step (b) is at least the same as the concentration of the alkaline solution in step (a). More preferably, the concentration of the acidic solution in step (b) is greater than the concentration of the alkaline solution in step (a).

根據本發明,將步驟(c)中之懸浮液過濾後所得濾物與析出之產物合併,乾燥後即可得到高純度之4,4'-二羧酸-2,2'-聯吡啶。According to the present invention, the filtrate obtained by filtering the suspension in the step (c) is combined with the precipitated product to obtain a high-purity 4,4'-dicarboxylic acid-2,2'-bipyridine.

根據本發明,純化4,4'-二羧酸-2,2'-聯吡啶之方法可在室溫下進行,不需加熱,可節省能源,更為環保。According to the present invention, the method for purifying 4,4'-dicarboxylic acid-2,2'-bipyridine can be carried out at room temperature, without heating, saving energy and being more environmentally friendly.

本發明純化方法可得到純度高達90%以上的4,4'-二羧酸-2,2'-聯吡啶。較佳地,4,4'-二羧酸-2,2'-聯吡啶的純度達到95%以上;更佳地,4,4'-二羧酸-2,2'-聯吡啶的純度達到98%,甚至99%,以上。The purification method of the present invention can obtain 4,4'-dicarboxylic acid-2,2'-bipyridine having a purity of up to 90% or more. Preferably, the purity of the 4,4'-dicarboxylic acid-2,2'-bipyridine is above 95%; more preferably, the purity of the 4,4'-dicarboxylic acid-2,2'-bipyridine is achieved. 98%, even 99%, above.

習知技術的純化方式須使用沸騰的硝酸,操作上甚為不便且有公共安全之風險。而產物經過一次純化過程後之純度仍不夠理想,即使經過第二、三次純化但純度已達極限(約85%)無法再提高。然而,本發明純化方法將酸化後的粗產物4,4'-二羧酸-2,2'-聯吡啶使用鹼及酸性溶液處理,不僅可得到純度高達90%以上的4,4'-二羧酸-2,2'-聯吡啶,且整個純化過程安全、便宜且無無污染。綜言之,本發明純化方法具有下列優點:The purification of conventional techniques requires the use of boiling nitric acid, which is inconvenient and at risk of public safety. The purity of the product after one purification process is still not ideal, even after the second and third purification, the purity has reached the limit (about 85%) can not be improved. However, the purification method of the present invention treats the acidified crude product 4,4'-dicarboxylic acid-2,2'-bipyridine using an alkali and an acidic solution, and can obtain not only 4,4'-di with a purity of more than 90%. Carboxylic acid-2,2'-bipyridine, and the entire purification process is safe, inexpensive and free of contamination. In summary, the purification method of the present invention has the following advantages:

(1) 原料為一般的鹼及酸性溶液,便宜且易取得。(1) The raw materials are general alkali and acidic solutions, which are cheap and easy to obtain.

(2) 純化過程產生之廢液可為中性,較不易對環境造成污染。(2) The waste liquid produced by the purification process can be neutral and less likely to cause environmental pollution.

(3) 純化過程不需加熱,在室溫中即可進行,相較之下較為安全,並可減少能源之消耗。(3) The purification process can be carried out at room temperature without heating, which is safer and reduces energy consumption.

(4) 所得到的4,4'-二羧酸-2,2'-聯吡啶具有高純度。(4) The obtained 4,4'-dicarboxylic acid-2,2'-bipyridine has high purity.

對照實例 4,4'-二羧酸-2,2'-聯吡啶之習知純化製程Comparative Example 4,4'-Dicarboxylic acid-2,2'-bipyridine conventional purification process

將5克未純化之粗產物4,4'-二羧酸-2,2'-聯吡啶與170毫升50%硝酸混合後,攪拌加熱至沸騰並持續4個小時。待反應裝置冷卻後,將溶液傾到入裝有冰塊之燒杯中再加水稀釋至1000毫升。將析出之固體過濾並以水(5×50毫升)沖洗至中性後,將之烘乾,純度85%。After 5 g of the unpurified crude product 4,4'-dicarboxylic acid-2,2'-bipyridine was mixed with 170 ml of 50% nitric acid, it was stirred and heated to boiling for 4 hours. After the reaction apparatus was cooled, the solution was poured into a beaker containing ice cubes and diluted with water to 1000 ml. The precipitated solid was filtered and washed with water (5 x 50 mL) until neutral, and then dried, with a purity of 85%.

實施例1本發明4,4'-二羧酸-2,2'-聯吡啶之純化製程Example 1 Purification Process of 4,4'-Dicarboxylic Acid-2,2'-Bipyridine of the Invention

將5克未純化之粗產物4,4'-二羧酸-2,2'-聯吡啶慢慢加入2M NaOH 50 ml溶液中,並在室溫下快速攪拌使固體完全溶解。接著用相同濃度之HCl 50 ml以滴定之方式加入混合液中使產物析出。過濾後將濾物烘乾即可得到純化之產物。上述製程如下列流程所示:5 g of the unpurified crude product 4,4'-dicarboxylic acid-2,2'-bipyridine was slowly added to a 2 M NaOH 50 ml solution, and rapidly stirred at room temperature to completely dissolve the solid. The mixture was then added to the mixture by titration with 50 ml of the same concentration of HCl to precipitate the product. After filtration, the filtrate is dried to obtain a purified product. The above process is shown in the following process:

上述純化過程後,得到之4,4'-二羧酸-2,2'-聯吡啶,其純度大於99%。4,4'-二羧酸-2,2'-聯吡啶之純度測試係由國立師範大學貴重儀器中心進行測試,使用氣相層析質譜儀(Finnigan TSQ-700 GC/LC/MS)、電子游離法(EI)及20電子伏特的離子化電壓。圖1顯示氣相層析質譜儀分析的測定結果,圖譜中243.9 m/z之訊號為主要分子離子峰:After the above purification process, 4,4'-dicarboxylic acid-2,2'-bipyridine is obtained with a purity of more than 99%. The purity test of 4,4'-dicarboxylic acid-2,2'-bipyridine was tested by the National Instruments Valuable Instrument Center using a gas chromatography mass spectrometer (Finnigan TSQ-700 GC/LC/MS), electronics. Free method (EI) and ionization voltage of 20 eV. Figure 1 shows the results of analysis by gas chromatography mass spectrometry. The signal of 243.9 m/z in the spectrum is the main molecular ion peak:

199.9 m/z之訊號為脫去一個羧酸分子之分子離子峰:The 199.9 m/z signal is the molecular ion peak from which a carboxylic acid molecule is removed:

155.1 m/z之訊號為脫去二個羧酸分子之分子離子峰:The 155.1 m/z signal is the molecular ion peak of the two carboxylic acid molecules removed:

圖1為本發明純化製程純化之4,4'-二羧酸-2,2'-聯吡啶的氣相層析質譜儀分析圖譜。1 is a gas chromatographic mass spectrometer analysis diagram of 4,4'-dicarboxylic acid-2,2'-bipyridine purified by the purification process of the present invention.

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Claims (8)

本發明提供一種純化4,4'-二羧酸-2,2'-聯吡啶之方法,其包括下列步驟:(a)使用鹼性溶液將不純之4,4'-二羧酸-2,2'-聯吡啶攪拌溶解;(b)將酸性溶液以滴定之方式加入所得混合液中,得到析出之產物,即純化之4,4'-二羧酸-2,2'-聯吡啶;及(c)過濾懸浮液並將過濾物與析出之產物合併,乾燥後即可得到高純度之4,4'-二羧酸-2,2'-聯吡啶;其中步驟(a)中之鹼性溶液為鹼金族氫氧化物溶液或氨水;及其中所得4,4'-二羧酸-2,2'-聯吡啶的純度高達95%以上。 The present invention provides a method for purifying 4,4'-dicarboxylic acid-2,2'-bipyridine, which comprises the steps of: (a) using an alkaline solution to impure 4,4'-dicarboxylic acid-2, 2'-bipyridine is dissolved and dissolved; (b) an acidic solution is added to the resulting mixture by titration to obtain a precipitated product, ie, purified 4,4'-dicarboxylic acid-2,2'-bipyridine; (c) filtering the suspension and combining the filtrate with the precipitated product, and drying to obtain high-purity 4,4'-dicarboxylic acid-2,2'-bipyridine; wherein the alkali in the step (a) The solution is an alkali gold hydroxide solution or ammonia water; and the purity of the obtained 4,4'-dicarboxylic acid-2,2'-bipyridine is as high as 95% or more. 如請求項1之方法,其中步驟(a)中之鹼性溶液為氫氧化鈉、氫氧化鉀、氫氧化鋰或氨水。 The method of claim 1, wherein the alkaline solution in the step (a) is sodium hydroxide, potassium hydroxide, lithium hydroxide or aqueous ammonia. 如請求項1之方法,其中步驟(a)中之鹼性溶液為氫氧化鈉。 The method of claim 1, wherein the alkaline solution in the step (a) is sodium hydroxide. 如請求項1之方法,其中步驟(b)中之酸性溶液為鹽酸、硝酸、硫酸及醋酸。 The method of claim 1, wherein the acidic solution in the step (b) is hydrochloric acid, nitric acid, sulfuric acid and acetic acid. 如請求項1之方法,其中步驟(b)中之酸性溶液為鹽酸。 The method of claim 1, wherein the acidic solution in the step (b) is hydrochloric acid. 如請求項1之方法,其中步驟(b)之酸性溶液滴定步驟後之溶液之pH值為中性。 The method of claim 1, wherein the pH of the solution after the acidic solution titration step of step (b) is neutral. 如請求項1之方法,其中所得4,4'-二羧酸-2,2'-聯吡啶的純度高達98%以上。 The method of claim 1, wherein the purity of the obtained 4,4'-dicarboxylic acid-2,2'-bipyridine is as high as 98% or more. 如請求項1之方法,其中所得4,4'-二羧酸-2,2'-聯吡啶的純度高達99%以上。The method of claim 1, wherein the purity of the obtained 4,4'-dicarboxylic acid-2,2'-bipyridine is as high as 99% or more.
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CN1374951A (en) * 1999-09-20 2002-10-16 日本曹达株式会社 Process for the preparation of 4(5)-amino-5(4) carboxamidoimidazoles and intermediates thereof

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1374951A (en) * 1999-09-20 2002-10-16 日本曹达株式会社 Process for the preparation of 4(5)-amino-5(4) carboxamidoimidazoles and intermediates thereof

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