TWI384073B - Method for producing bioethanol from fiber product containing cellulose - Google Patents

Method for producing bioethanol from fiber product containing cellulose Download PDF

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TWI384073B
TWI384073B TW097150544A TW97150544A TWI384073B TW I384073 B TWI384073 B TW I384073B TW 097150544 A TW097150544 A TW 097150544A TW 97150544 A TW97150544 A TW 97150544A TW I384073 B TWI384073 B TW I384073B
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cellulose
producing
fibrous product
containing fibrous
alcohol
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TW201024418A (en
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Po Ju Lin
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Taiwan Textile Res Inst
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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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

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Description

以含纖維素的纖維製品為原料生產生質酒精的方法Method for producing quality alcohol by using cellulose-containing fiber products as raw materials

本發明是有關於一種生產生質酒精(bioethanol)的方法,且特別是有關於一種以含纖維素(cellulose)的纖維製品(fiber product)為原料生產生質酒精的方法。This invention relates to a process for producing bioethanol, and more particularly to a process for producing a quality alcohol from a cellulose-containing fiber product.

隨著科技與經濟的發展,人類社會對於能源的需求與日俱增。然而目前所仰賴的能源,例如石油、天然氣或燃煤等皆為污染性能源,過度地使用除了會帶來汙染,導致環境的破壞日益嚴重之外,這些污染性能源也逐漸面臨到短缺的問題。因此,無污染且可再生的能源越來越受到重視。With the development of technology and economy, the demand for energy in human society is increasing day by day. However, the energy currently relied on, such as oil, natural gas or coal, is a polluting energy source. Excessive use will lead to shortages in addition to pollution and environmental damage. . Therefore, pollution-free and renewable energy sources are receiving more and more attention.

所謂的再生能源(renewable energy)是指理論上可以取之不盡的天然能源,例如太陽能、風能、水力、地熱或是生質能(biomass energy)等。其中,關於生質能的利用更是近年來相當重要且受歡迎的議題。所謂生質能,是指從多樣化生物所產生的有機物質(亦即生質)中提取,經過各種天然或人為之化學反應轉化以後,可直接或間接地作為能源使用者。簡言之,生質能是以生物產生的有機物質作為能源,故其無毒且可分解,因而被視為一種重要之綠色能源。The so-called renewable energy refers to the natural energy that can theoretically be inexhaustible, such as solar energy, wind energy, hydropower, geothermal energy or biomass energy. Among them, the use of biomass energy is a very important and popular topic in recent years. The so-called biomass energy refers to the extraction of organic matter (that is, biomass) produced by diverse organisms. After being transformed by various natural or artificial chemical reactions, it can be directly or indirectly used as an energy user. In short, biomass can be regarded as an important green energy source because it is a biologically produced organic substance as an energy source, so it is non-toxic and decomposable.

一般而言,生質能之利用是採取醣類發酵方式,將生質轉換成酒精。第一代生質酒精是利用穀物及蔗糖等糧食作物為原料所生產,其缺點在於可能造成能源消耗以及與糧食需求競合。第二代生質酒精是利用稻稈、玉米稈、蔗渣或木屑等含纖維之農業廢棄物為原料所生產,故又稱為纖維酒精,其充分利用農業廢棄物以及非糧食之能源作物,但缺點在於前處理較為複雜耗時,而且回收率不高。In general, the utilization of biomass energy is a sugar fermentation method that converts biomass into alcohol. The first generation of raw alcohol was produced from food crops such as grains and sucrose, which had the disadvantage of causing energy consumption and competing with food demand. The second generation of raw alcohol is produced by using fibrous waste agricultural waste such as rice straw, corn stalk, bagasse or sawdust, so it is also called fiber alcohol, which makes full use of agricultural waste and non-food energy crops, but The disadvantage is that the pre-processing is more complicated and time-consuming, and the recovery rate is not high.

在實務上,如何妥善利用含纖維素之纖維製品,進一步又能簡化製程,降低纖維素提取分離之難度,並提高終產物之產率或回收率,實為目前纖維素生質酒精之生產技術上亟待克服的課題。In practice, how to properly use cellulose-containing fiber products can further simplify the process, reduce the difficulty of cellulose extraction and separation, and improve the yield or recovery rate of the final product. This is the current production technology of cellulose bio-alcohol. The subject to be overcome.

本發明提供一種以含纖維素的纖維製品為原料生產生質酒精的方法,其以酸性溶液提取原料中的纖維素,再以非溶劑將纖維素析出。The present invention provides a method for producing a quality alcohol by using a cellulose-containing fibrous product as a raw material, which extracts cellulose in a raw material with an acidic solution, and then precipitates the cellulose by a non-solvent.

本發明提出一種以含纖維素的纖維製品為原料生產生質酒精的方法,其包括下列步驟。首先,將一含纖維素的纖維製品溶解於一酸性溶液中。次之,進行一第一過濾程序,以取得含有纖維素的一過濾液。再者,在過濾液中加入一非溶劑,以使過濾液中的纖維素析出。接著,進行一第二過濾程序,以取得析出的纖維素。最後,進行一酵素水解(enzymatic hydrolysis)及發酵程序,以使纖維素轉化成糖及酒精。The present invention provides a method for producing a quality alcohol from a cellulose-containing fibrous product, which comprises the following steps. First, a cellulose-containing fibrous product is dissolved in an acidic solution. Next, a first filtration process is performed to obtain a filtrate containing cellulose. Further, a non-solvent is added to the filtrate to precipitate cellulose in the filtrate. Next, a second filtration process is performed to obtain the precipitated cellulose. Finally, an enzymatic hydrolysis and fermentation process is carried out to convert the cellulose into sugar and alcohol.

在本發明之一實施例中,上述含纖維素的纖維製品包括一含棉製品或紙張。In an embodiment of the invention, the cellulose-containing fibrous article comprises a cotton-containing article or paper.

在本發明之一實施例中,上述含棉製品包括一紡織品(textile)、一不織布(non-woven fabric)或是紗線(yarn)。In one embodiment of the invention, the cotton-containing article comprises a textile, a non-woven fabric or a yarn.

在本發明之一實施例中,上述含纖維素的纖維製品為一廢棄的(waste)含纖維素的纖維製品。In one embodiment of the invention, the cellulose-containing fibrous article is a waste cellulose-containing fibrous article.

在本發明之一實施例中,上述之酸性溶液包括磷酸(Phosphoric Acid)溶液、硫酸(Sulfuric Acid)溶液或是鹽酸(Hydrochloric Acid)溶液。In an embodiment of the invention, the acidic solution comprises a Phosphoric Acid solution, a Sulfuric Acid solution or a Hydrochloric Acid solution.

在本發明之一實施例中,上述之酸性溶液的重量百分比濃度為30~90%。In an embodiment of the invention, the above-mentioned acidic solution has a concentration by weight of 30 to 90%.

在本發明之一實施例中,上述含纖維素的纖維製品溶解於酸性溶液中之步驟是在攝氏50~90度的溫度條件中進行10分鐘至3小時。In an embodiment of the present invention, the step of dissolving the cellulose-containing fibrous product in an acidic solution is carried out at a temperature of 50 to 90 ° C for 10 minutes to 3 hours.

在本發明之一實施例中,上述之非溶劑包括水或是丙酮(Acetone)。In one embodiment of the invention, the non-solvent described above comprises water or acetone (Acetone).

在本發明之一實施例中,上述之非溶劑的使用量與酸性溶液使用量的比例為0.1:1~10:1。In one embodiment of the present invention, the ratio of the amount of the non-solvent used to the amount of the acidic solution used is from 0.1:1 to 10:1.

在本發明之一實施例中,上述以含纖維素的纖維製品為原料生產生質酒精的方法,其中於進行第一過濾程序之後,更包括進行一回收聚酯(polyester,PET)之步驟。In an embodiment of the invention, the method for producing a quality alcohol by using the cellulose-containing fiber product as a raw material, further comprising the step of recovering polyester (PET) after performing the first filtering process.

在本發明之一實施例中,上述以含纖維素的纖維製品為原料生產生質酒精的方法,其中於進行第二過濾程序之後,更包括進行一回收非溶劑之步驟。In an embodiment of the present invention, the method for producing a quality alcohol by using the cellulose-containing fibrous product as a raw material, further comprising the step of recovering the non-solvent after performing the second filtering step.

在本發明之一實施例中,上述之以含纖維素的纖維製品為原料生產生質酒精的方法,其中於進行第二過濾程序以取得析出的纖維素之後,更包括進行一洗滌程序。In one embodiment of the present invention, the method for producing a quality alcohol by using a cellulose-containing fibrous product as described above, wherein after performing the second filtration process to obtain the precipitated cellulose, further comprises performing a washing procedure.

在本發明之一實施例中,上述之酵素水解及發酵程序所使用的酵素包括一內切型纖維分解酵素、一外切型纖維分解酵素以及一纖維雙醣或纖維寡糖水解酵素。In one embodiment of the present invention, the enzyme used in the enzyme hydrolysis and fermentation process includes an endo-type fibrinolytic enzyme, an exo-type fibrinolytic enzyme, and a cellobiose or cellooligosaccharide hydrolase.

在本發明之一實施例中,上述之以含纖維素的纖維製品為原料生產生質酒精的方法,在進行酵素水解及發酵程序之前不進行高溫殺菌程序。In one embodiment of the present invention, the above method for producing a quality alcohol using a cellulose-containing fibrous product as a raw material does not perform a high-temperature sterilization process before the enzyme hydrolysis and fermentation process.

基於上述,本發明之生產生質酒精的方法是以含纖維素之纖維製品為原料,以酸性溶液同時進行原料的前處理以及纖維素成份的溶解,再加入不能溶解纖維素之非溶劑將纖維素飽和析出。因此本發明之方法相較於傳統方法較為簡化且無需特殊篩選的菌種,即可將原料中的纖維素提取與分解。Based on the above, the method for producing a quality alcohol according to the present invention is to use a cellulose-containing fibrous product as a raw material, to simultaneously pretreat the raw material with an acidic solution, and to dissolve the cellulose component, and then add the non-solvent which cannot dissolve the cellulose to the fiber. The protein is saturated and precipitated. Therefore, the method of the present invention can extract and decompose cellulose in the raw material as compared with the conventional method, which is simpler and does not require a specially selected strain.

為讓本發明之上述特徵和優點能更明顯易懂,下文特舉實施例,並配合所附圖式作詳細說明如下。The above described features and advantages of the present invention will be more apparent from the following description.

圖1為根據本發明之一實施例之以含纖維素的纖維製品為原料生產生質酒精的方法流程圖。請參照圖1,其包括下列步驟。首先,進行步驟110,將一含纖維素的纖維製品溶解於一酸性溶液中。上述之含纖維素的纖維製品例如是一含棉製品、紙張或是其他適當的含纖維素材料,其中含棉製品例如是一紡織品、一不織布或是紗線。在本實施例中,含纖維素的纖維製品是一廢棄的含纖維素的纖維製品,例如是回收的紙張、回收的舊衣、廢棄的布料或是紗線等。BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a flow chart showing a method for producing a quality alcohol from a cellulose-containing fibrous product according to an embodiment of the present invention. Please refer to FIG. 1, which includes the following steps. First, in step 110, a cellulose-containing fibrous product is dissolved in an acidic solution. The above cellulose-containing fibrous product is, for example, a cotton-containing product, paper or other suitable cellulose-containing material, wherein the cotton-containing product is, for example, a textile, a nonwoven fabric or a yarn. In the present embodiment, the cellulose-containing fibrous product is a waste cellulose-containing fibrous product such as recycled paper, recycled old clothes, discarded cloth or yarn.

由於纖維素具有耐鹼不耐酸的特性,故在適當的酸液處理下,纖維素會溶解於酸液之中。在本實施例中,酸性溶液例如是磷酸溶液、硫酸溶液、鹽酸溶液、硝酸溶液或是其他適當的酸性溶液,其重量百分比濃度大致介於30~90%之間。若以工業上常用且易取得的觀點而言,上述之酸性溶液是選用85%的磷酸溶液。而且此一溶解步驟110是在攝氏50~90度的溫度條件中進行10分鐘至3小時。Since cellulose has an alkali-resistant and acid-resistant property, cellulose is dissolved in an acid solution under appropriate acid treatment. In the present embodiment, the acidic solution is, for example, a phosphoric acid solution, a sulfuric acid solution, a hydrochloric acid solution, a nitric acid solution or other suitable acidic solution, and the concentration by weight is approximately between 30 and 90%. The above acidic solution is an 85% phosphoric acid solution from the viewpoint of industrially common and readily available. Further, this dissolution step 110 is carried out at a temperature of 50 to 90 degrees Celsius for 10 minutes to 3 hours.

值得一提的是,本發明並不特別限制上述酸性溶液的種類、重量百分比濃度、溶解之溫度條件以及進行時間。換言之,在不同的酸性溶液種類、重量百分比濃度、溫度條件以及進行時間下,亦可能有相同或相近的表現,本領域具有通常知識者可以根據所需的結果適當地自行調整。It is to be noted that the present invention does not particularly limit the kind of the above acidic solution, the concentration by weight, the temperature conditions for dissolution, and the progress time. In other words, the same or similar performance may be present under different acidic solution types, weight percentage concentrations, temperature conditions, and time of conduct, and those having ordinary knowledge in the art may appropriately adjust themselves according to the desired result.

圖2為本發明一實施例之磷酸前處理與有無去色對纖維素水解之影響的實驗結果。圖3為本發明一實施例之染料及去色對糖發酵成酒精之抑制性的實驗結果。為了釐清本實施例使用的含纖維素之纖維製品若經過染色,對於磷酸水解效果是否有影響,因而進行了以下的實驗。請先參照圖2,將以磷酸分別處理廢棉布、去色廢布以及有色廢布三組實驗的數據,與未以磷酸處理廢棉布、去色廢布以及有色廢布三組實驗的數據合併比較。在圖2中,橫軸表示時間,縱軸表示糖濃度,糖濃度越高表示水解效果越佳。從圖2中的結果可清楚得知,經磷酸溶液前處理的水解效果明顯優於未加磷酸單純水解的效果,而使用廢棉布作為原料的效果又依序略高於去色廢布以及有色廢布。接著,請參照圖3,在圖3中,橫軸表示時間,縱軸表示糖濃度,糖濃度隨時間越低表示發酵效果越佳。從圖3的結果可清楚得知,本實施例中染料及去色之處理對糖發酵作用的抑制性並不顯著。2 is an experimental result of the effect of pretreatment of phosphoric acid and the presence or absence of decoloration on hydrolysis of cellulose according to an embodiment of the present invention. Fig. 3 is a graph showing the results of an experiment for inhibiting the dyeing of sugar into alcohol by an example of the dye and the decolorization of the present invention. In order to clarify whether the cellulose-containing fibrous product used in the present example was dyed, whether it had an effect on the phosphoric acid hydrolysis effect, the following experiment was conducted. Please refer to Figure 2 first, and combine the data of three sets of experiments of treating waste cotton cloth, decolorized waste cloth and colored waste cloth with phosphoric acid, and data of three sets of experiments without using phosphoric acid treated waste cotton cloth, decolorized waste cloth and colored waste cloth. Comparison. In Fig. 2, the horizontal axis represents time, and the vertical axis represents sugar concentration, and the higher the sugar concentration, the better the hydrolysis effect. It can be clearly seen from the results in Fig. 2 that the hydrolysis effect by the phosphoric acid solution pretreatment is obviously better than that of the un-phosphoric acid alone, and the effect of using waste cotton cloth as a raw material is slightly higher than that of the decolorized waste cloth and the colored Waste cloth. Next, referring to Fig. 3, in Fig. 3, the horizontal axis represents time, the vertical axis represents sugar concentration, and the lower the sugar concentration with time, the better the fermentation effect. As is clear from the results of Fig. 3, the dye and the treatment of decolorization in this example have no significant inhibition on the sugar fermentation.

請再參照圖1,接著,進行步驟120,進行一第一過濾程序,以取得含有纖維素的一過濾液(filtrate)。在步驟110完成之後,纖維製品中所含的纖維素會溶解於前述酸性溶液中,故於此時實施一過濾程序,以分離含有纖維素之過濾液以及不溶於酸性溶液之其他成分。前述過濾方法可以是一般篩網過濾、濾紙過濾、離心過濾或其他可能之過濾方法,本領域具有通常知識者可以適當地自行調整。Referring again to FIG. 1, then, in step 120, a first filtration process is performed to obtain a filtrate containing cellulose. After the completion of the step 110, the cellulose contained in the fibrous product is dissolved in the acidic solution, and at this time, a filtration procedure is carried out to separate the cellulose-containing filtrate and other components insoluble in the acidic solution. The foregoing filtration method may be general screen filtration, filter paper filtration, centrifugal filtration or other possible filtration methods, and those skilled in the art may appropriately adjust themselves.

在本實施例中,於進行第一過濾程序之後,更包括進行一回收聚酯(polyester,PET)之步驟160。聚酯是一種常見的人造纖維原料,可以製成聚酯絲單獨製作成衣物,也可以與棉、麻、毛等各項天然纖維混紡製作成織物(textile)。聚酯的應用在現代紡織與成衣行業裡已經非常普遍。由於聚酯有著耐酸不耐鹼的特性,故在前述溶解步驟110的酸處理之後,被溶解於酸液之中的纖維素與過濾液一起被收集,遺留下來的成分即含有不溶於酸之聚酯成分。這些含有聚酯成分的混合物經過處理可進一步回收,以提昇含纖維素原料之整體利用性。In this embodiment, after performing the first filtering process, a step 160 of recovering polyester (PET) is further included. Polyester is a common raw material of man-made fiber. It can be made into polyester yarn separately, or it can be blended with natural fibers such as cotton, hemp and wool to make a textile. The use of polyester has become very common in the modern textile and ready-to-wear industry. Since the polyester has acid and alkali resistance characteristics, after the acid treatment in the dissolution step 110 described above, the cellulose dissolved in the acid solution is collected together with the filtrate, and the remaining components contain the acid-insoluble aggregate. Ester component. These polyester-containing mixtures can be further processed to improve the overall utilization of the cellulose-containing raw materials.

再者,進行步驟130,在過濾液中加入一非溶劑,以使過濾液中的纖維素析出。步驟120中被收集之過濾液含有溶於酸液中的纖維素,故再加入對纖維素不溶解之溶液,亦即此處所謂之非溶劑,以使纖維素於溶液中過飽和而(沉澱)析出。在本實施例中,非溶劑例如是水、丙酮或是其他適當之溶液,且非溶劑使用量與酸性溶液使用量的比例為0.1:1~10:1。值得一提的是,本發明並不特別限制上述非溶劑使用量與酸性溶液使用量的比例為0.1:1~10:1。換言之,在其他的比例之下,亦可能有相同或相近的纖維素析出表現,本領域具有通常知識者可以適當自行調整。Further, in step 130, a non-solvent is added to the filtrate to precipitate the cellulose in the filtrate. The filtrate collected in step 120 contains cellulose dissolved in the acid solution, so a solution which is insoluble to cellulose, that is, a non-solvent as described herein, is added to supersaturate the cellulose in the solution (precipitation). Precipitate. In the present embodiment, the non-solvent is, for example, water, acetone or other suitable solution, and the ratio of the amount of the non-solvent used to the amount of the acidic solution used is from 0.1:1 to 10:1. It is to be noted that the present invention does not particularly limit the ratio of the amount of the non-solvent used to the amount of the acidic solution used in the range of 0.1:1 to 10:1. In other words, under other ratios, it is also possible to have the same or similar cellulose precipitation performance, and those skilled in the art can appropriately adjust themselves.

之後,進行步驟140,進行一第二過濾程序,以取得步驟130析出的纖維素。吾人可藉由一般篩網過濾、濾紙過濾、離心過濾或其他可能之過濾方法,取得步驟130中被析出的纖維素。在本實施例中,過濾後析出的纖維素更可以包括進行一洗滌程序170,洗滌的溶液可以是蒸餾水。Thereafter, in step 140, a second filtration process is performed to obtain the cellulose precipitated in step 130. The cellulose precipitated in step 130 can be obtained by conventional screen filtration, filter paper filtration, centrifugal filtration or other possible filtration methods. In this embodiment, the cellulose precipitated after filtration may further comprise performing a washing procedure 170, and the washed solution may be distilled water.

於進行第二過濾程序140之後,可進一步進行一回收非溶劑之步驟180。若上述步驟130所使用的非溶劑是丙酮或是其他溶液,那麼回收之後亦可用於步驟130中。After the second filtration process 140 is performed, a step 180 of recovering the non-solvent may be further performed. If the non-solvent used in the above step 130 is acetone or other solution, it can be used in step 130 after recovery.

最後,進行步驟150,進行一酵素水解及發酵程序,以使纖維素轉化成糖及酒精。在本實施例中,酵素水解及發酵程序所使用的酵素包括一內切型纖維分解酵素(例如是endo-β-1,4 glucanase)、一外切型纖維分解酵素(例如是exo-β-1,4 glucanase)以及一纖維雙醣或纖維寡糖水解酵素(例如是β-glucosidase)。內切型纖維分解酵素主要作用於纖維素的非結晶區,將纖維素的β-1,4配醣鍵(β-1,4 glucosidic bond)以隨機方式分解。外切型纖維分解酵素主要作用由纖維素的結晶區的非還原端(non-reducing end)開始以纖維雙醣為單位分解,產生纖維雙糖。纖維寡糖水解酵素則自非還原端起將纖維雙醣或纖維寡糖水解成葡萄糖。Finally, step 150 is performed to perform an enzyme hydrolysis and fermentation process to convert the cellulose into sugar and alcohol. In the present embodiment, the enzyme used in the enzyme hydrolysis and fermentation process includes an endo-type fibrinolytic enzyme (for example, endo-β-1, 4 glucanase) and an exo-type fibrinolytic enzyme (for example, exo-β- 1,4 glucanase) and a cellobiose or cellooligosaccharide hydrolase (for example, β-glucosidase). The endo-type fibrinolytic enzyme mainly acts on the amorphous region of cellulose, and decomposes the β-1,4 glucosidic bond of cellulose in a random manner. The external action of the exo-type fibrinolytic enzyme starts from the non-reducing end of the crystalline region of cellulose and is decomposed in units of cell disaccharide to produce a cell disaccharide. The cellooligosaccharide hydrolase hydrolyzes cellobiose or cellooligosaccharide to glucose from the non-reducing end.

圖4為磷酸前處理、纖維素來源與染色及去色對酵素水解之影響的實驗結果。請參照圖4,在圖4中,橫軸表示時間,縱軸表示糖濃度,糖濃度越高表示酵素水解效果越佳。將磷酸處理之棉花、廢棉布、染色廢布、去色廢布、混紡廢布以及去色混紡廢布,與未經磷酸處理之棉花、廢棉布、染色廢布、去色廢布、混紡廢布以及去色混紡廢布的酵素水解實驗數據作合併比較。從圖4的結果可清楚得知,本實施例中添加磷酸溶液的水解效果明顯優於未加磷酸單純水解的效果,使用棉花或精練布作為原料的效果又依序高於色棉布及脫色布、色混紡布及脫色布,但差異不大,且在5~10小時內即可水解完全,一般木質纖維素則需要1.5~2天。Figure 4 shows the experimental results of the effects of phosphoric acid pretreatment, cellulose source and dyeing, and decolorization on enzyme hydrolysis. Referring to Fig. 4, in Fig. 4, the horizontal axis represents time, and the vertical axis represents sugar concentration, and the higher the sugar concentration, the better the enzyme hydrolysis effect. Phosphoric acid treated cotton, waste cotton cloth, dyed waste cloth, decolorized waste cloth, blended waste cloth and decolorized blended waste cloth, and non-phosphoric acid treated cotton, waste cotton cloth, dyed waste cloth, decolorized waste cloth, blended waste The enzyme hydrolysis test data of the cloth and the decolorized blend waste cloth were compared and compared. It can be clearly seen from the results of FIG. 4 that the hydrolysis effect of the phosphoric acid solution added in this embodiment is obviously better than that of the simple hydrolysis without the addition of phosphoric acid, and the effect of using cotton or scouring cloth as a raw material is higher than that of the color cotton cloth and the bleaching cloth. , color blended fabric and bleaching cloth, but the difference is not big, and it can be hydrolyzed completely within 5~10 hours, generally lignocellulose takes 1.5~2 days.

值得一提的是,在本實施例中,於進行酵素水解及發酵程序之前不進行高溫殺菌程序。由於葡萄醣與氮源混合高溫滅菌時會造成梅納反應(Maillard reaction),使得部分葡萄醣不被菌體代謝,因而影響到終產品酒精的回收率。圖5A及圖5B分別為廢棉布以及染色廢棉布不經高溫殺菌直接同步發酵的實驗結果。請參照圖5A及圖5B,在圖5A及圖5B中,橫軸表示時間,縱軸表示酒精產量。從圖5A的結果可清楚得知,未染色的廢棉布酒精產量約為43.4g/L,轉化率為0.42g EtOH/g glucose。從圖5B的結果可清楚得知,染色廢棉布酒精產量為約47.7g/L,轉化率為0.43g EtOH/g glucose。It is worth mentioning that in this embodiment, the high temperature sterilization process is not performed until the enzyme hydrolysis and fermentation process. Due to the high temperature sterilization of glucose and nitrogen source, the Maillard reaction is caused, so that part of the glucose is not metabolized by the bacteria, thus affecting the recovery rate of the final product alcohol. 5A and 5B are experimental results of direct synchronous fermentation of waste cotton cloth and dyed waste cotton cloth without high temperature sterilization. Referring to FIGS. 5A and 5B, in FIGS. 5A and 5B, the horizontal axis represents time and the vertical axis represents alcohol production. As is clear from the results of Fig. 5A, the undyed waste cotton cloth had an alcohol yield of about 43.4 g/L and a conversion of 0.42 g EtOH/g glucose. As is clear from the results of Fig. 5B, the dyed waste cotton cloth had an alcohol yield of about 47.7 g/L and a conversion rate of 0.43 g EtOH/g glucose.

另外,以下提供發酵前高溫殺菌處理和不高溫殺菌處理的測試數據於表1。由同時參考圖5A、5B與表1可清楚得知,發酵前不經高溫殺菌處理可得較高的酒精轉化率。In addition, the following test data for providing high temperature sterilization treatment and non-high temperature sterilization treatment before fermentation are shown in Table 1. It can be clearly seen from the same reference to Figs. 5A, 5B and Table 1 that high alcohol conversion rate can be obtained without high temperature sterilization treatment before fermentation.

綜上所述,本發明之以含纖維素之纖維製品為原料生產生質酒精的方法,係以酸性溶液進行纖維素成分之溶解,又因纖維製品內之纖維素不含木質素及其他醣類,故其酒精產生速度較快,轉化率較高。其次,纖維素成份在溶解提取後不需高溫殺菌,除可減少作業時間,更能進一步提高終產品(酒精)之回收率。另外,於過濾提取纖維素成份之同時亦可以分離及回收聚酯,故能將原材料更進一步地回收利用。In summary, the method for producing a quality alcohol by using a cellulose-containing fiber product as a raw material is to dissolve the cellulose component by an acidic solution, and because the cellulose in the fiber product does not contain lignin and other sugars. Class, so its alcohol production rate is faster, and the conversion rate is higher. Secondly, the cellulose component does not need to be sterilized after being dissolved and extracted, in addition to reducing the working time, and further improving the recovery rate of the final product (alcohol). In addition, the polyester can be separated and recovered while filtering and extracting the cellulose component, so that the raw material can be further recycled.

雖然本發明已以實施例揭露如上,然其並非用以限定本發明,任何所屬技術領域中具有通常知識者,在不脫離本發明之精神和範圍內,當可作些許之更動與潤飾,故本發明之保護範圍當視後附之申請專利範圍所界定者為準。Although the present invention has been disclosed in the above embodiments, it is not intended to limit the invention, and any one of ordinary skill in the art can make some modifications and refinements without departing from the spirit and scope of the invention. The scope of the invention is defined by the scope of the appended claims.

110...將一含纖維素的纖維製品溶解於一酸性溶液中110. . . Dissolving a cellulose-containing fibrous product in an acidic solution

120...進行一第一過濾程序,以取得含有纖維素的一過濾液120. . . Performing a first filtration process to obtain a filtrate containing cellulose

130...加入一非溶劑,使過濾液中的纖維素析出130. . . Adding a non-solvent to precipitate cellulose in the filtrate

140...進行一第二過濾程序,以取得析出的纖維素140. . . Perform a second filtration process to obtain precipitated cellulose

150...進行一酵素水解及發酵程序,使纖維素轉化成糖及酒精150. . . Perform an enzyme hydrolysis and fermentation process to convert cellulose into sugar and alcohol

160...進行一回收聚酯之步驟160. . . Carry out a step of recycling the polyester

170...進行一纖維素之洗滌程序170. . . Carrying out a cellulose washing procedure

180...進行一回收酸性溶液及非溶劑之步驟180. . . Carry out a step of recovering the acidic solution and the non-solvent

圖1為本發明之一種以含纖維素的纖維製品為原料生產生質酒精的方法流程圖。BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a flow chart showing a method for producing a quality alcohol by using a cellulose-containing fibrous product as a raw material.

圖2為本發明之一實施例之磷酸前處理與染色之影響的實驗結果。2 is an experimental result of the effects of phosphoric acid pretreatment and dyeing according to an embodiment of the present invention.

圖3為本發明之一實施例之染料及去色對糖發酵成酒精之抑制性的實驗結果。Figure 3 is a graph showing the results of experiments on the inhibition of dyeing and decolorization of sugars into alcohol by an embodiment of the present invention.

圖4為本發明之一實施例之磷酸前處理、纖維素來源與染色對酵素水解之影響的實驗結果。4 is an experimental result of the effect of pre-treatment of phosphoric acid, cellulose source and dyeing on hydrolysis of an enzyme according to an embodiment of the present invention.

圖5A及圖5B分別為廢棉布以及染色廢棉布不經高溫殺菌直接同步發酵的實驗結果。5A and 5B are experimental results of direct synchronous fermentation of waste cotton cloth and dyed waste cotton cloth without high temperature sterilization.

110...將一含纖維素的纖維製品溶解於一酸性溶液中110. . . Dissolving a cellulose-containing fibrous product in an acidic solution

120...進行一第一過濾程序,以取得含有纖維素的一過濾液120. . . Performing a first filtration process to obtain a filtrate containing cellulose

130...加入一非溶劑,使過濾液中的纖維素析出130. . . Adding a non-solvent to precipitate cellulose in the filtrate

140...進行一第二過濾程序,以取得析出的纖維素140. . . Perform a second filtration process to obtain precipitated cellulose

150...進行一酵素水解及發酵程序,使纖維素轉化成糖及酒精150. . . Perform an enzyme hydrolysis and fermentation process to convert cellulose into sugar and alcohol

160...進行一回收聚酯之步驟160. . . Carry out a step of recycling the polyester

170...進行一纖維素之洗滌程序170. . . Carrying out a cellulose washing procedure

180...進行一回收酸性溶液及非溶劑之步驟180. . . Carry out a step of recovering the acidic solution and the non-solvent

Claims (11)

一種以含纖維素的纖維製品為原料生產生質酒精的方法,包括:將一含纖維素的纖維製品溶解於一酸性溶液中,其中該含纖維素的纖維製品包括一含棉製品或紙張、或是一廢棄的含纖維素的纖維製品;進行一第一過濾程序,以取得含有纖維素的一過濾液;於進行該第一過濾程序之後,更包括進行一回收聚酯之步驟;在該過濾液中加入一非溶劑,以使該過濾液中的纖維素析出;進行一第二過濾程序,以取得析出的纖維素;以及進行一酵素水解及發酵程序,以使該纖維素轉化成糖及酒精。 A method for producing a quality alcohol by using a cellulose-containing fibrous product, comprising: dissolving a cellulose-containing fibrous product in an acidic solution, wherein the cellulose-containing fibrous product comprises a cotton-containing product or paper, Or a waste cellulose-containing fibrous product; performing a first filtration process to obtain a filtrate containing cellulose; and after performing the first filtration process, further comprising the step of recovering the polyester; Adding a non-solvent to the filtrate to precipitate cellulose in the filtrate; performing a second filtration process to obtain precipitated cellulose; and performing an enzyme hydrolysis and fermentation process to convert the cellulose into sugar And alcohol. 如申請專利範圍第1項所述之以含纖維素的纖維製品為原料生產生質酒精的方法,其中該含棉製品包括一紡織品、一不織布或是紗線。 The method for producing a quality alcohol by using a cellulose-containing fibrous product as described in claim 1, wherein the cotton-containing product comprises a textile, a non-woven fabric or a yarn. 如申請專利範圍第1項所述之以含纖維素的纖維製品為原料生產生質酒精的方法,其中該酸性溶液包括磷酸溶液、硫酸溶液或是鹽酸溶液。 The method for producing a quality alcohol by using a cellulose-containing fibrous product as described in claim 1, wherein the acidic solution comprises a phosphoric acid solution, a sulfuric acid solution or a hydrochloric acid solution. 如申請專利範圍第3項所述之以含纖維素的纖維製品為原料生產生質酒精的方法,其中該酸性溶液的濃度為30~90 wt%。 A method for producing a quality alcohol by using a cellulose-containing fibrous product as described in claim 3, wherein the concentration of the acidic solution is 30 to 90 wt%. 如申請專利範圍第1項所述之以含纖維素的纖維製品為原料生產生質酒精的方法,其中將該含纖維素的纖維製品溶解於該酸性溶液中之步驟是在攝氏50~90度的溫度條件中進行10分鐘至3小時。 The method for producing a quality alcohol by using a cellulose-containing fibrous product as described in claim 1, wherein the step of dissolving the cellulose-containing fibrous product in the acidic solution is at 50 to 90 degrees Celsius. The temperature is carried out for 10 minutes to 3 hours. 如申請專利範圍第1項所述之以含纖維素的纖維製品為原料生產生質酒精的方法,其中該非溶劑包括水或是丙酮。 A method for producing a quality alcohol by using a cellulose-containing fibrous product as described in claim 1, wherein the non-solvent comprises water or acetone. 如申請專利範圍第1項所述之以含纖維素的纖維製品為原料生產生質酒精的方法,其中該非溶劑的使用量與該酸性溶液使用量的比例為0.1:1~10:1。 The method for producing a quality alcohol by using a cellulose-containing fiber product as described in claim 1, wherein the ratio of the non-solvent used to the acidic solution is 0.1:1 to 10:1. 如申請專利範圍第1項所述之以含纖維素的纖維製品為原料生產生質酒精的方法,其中於進行該第二過濾程序之後,更包括進行一回收非溶劑之步驟。 The method for producing a quality alcohol by using a cellulose-containing fibrous product as described in claim 1, wherein after the second filtering step, the step of recovering the non-solvent is further included. 如申請專利範圍第1項所述之以含纖維素的纖維製品為原料生產生質酒精的方法,其中於進行該第二過濾程序以取得析出的纖維素之後,更包括進行一洗滌程序。 The method for producing a quality alcohol by using a cellulose-containing fibrous product as described in claim 1, wherein after performing the second filtration process to obtain precipitated cellulose, a washing process is further included. 如申請專利範圍第1項所述之以含纖維素的纖維製品為原料生產生質酒精的方法,其中該酵素水解程序所使用的酵素包括一內切型纖維分解酵素、一外切型纖維分解酵素以及一纖維雙醣或纖維寡糖水解酵素。 The method for producing a quality alcohol by using a cellulose-containing fiber product as described in claim 1, wherein the enzyme used in the enzyme hydrolysis process comprises an endo-type fibrinolytic enzyme and an exo-type fiber decomposition. Enzyme and a cellobiose or cellooligosaccharide hydrolase. 如申請專利範圍第1項所述之以含纖維素的纖維製品為原料生產生質酒精的方法,其中在進行該酵素水解及發酵程序之前不進行高溫殺菌程序。A method for producing a quality alcohol by using a cellulose-containing fibrous product as described in claim 1, wherein the high temperature sterilization process is not performed before the enzyme hydrolysis and fermentation process.
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* Cited by examiner, † Cited by third party
Title
永續產業資訊雙月刊,第三十五期,第6~15頁,96.10.15。網址:http://www.ema.org.tw/monthlymgz/pdf/35/6-15.pdf 簡宣裕、張明暉、劉禎祺,木質纖維素產生能源方法之探討。 *
綠色油田在農業永續發展扮演的角色: 103-113,農業試驗所特刊第132號,2007年12月,網址: http://www.tari.gov.tw/taric/uploads/publication_no132_12.pdf 201024418 99/07/01 *
陳建孝 林畢修平,纖維酒精製程簡介與未來展望。 *

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