TWI690497B - A power system of biofuel and the operating method thereof - Google Patents
A power system of biofuel and the operating method thereof Download PDFInfo
- Publication number
- TWI690497B TWI690497B TW108100122A TW108100122A TWI690497B TW I690497 B TWI690497 B TW I690497B TW 108100122 A TW108100122 A TW 108100122A TW 108100122 A TW108100122 A TW 108100122A TW I690497 B TWI690497 B TW I690497B
- Authority
- TW
- Taiwan
- Prior art keywords
- power generation
- waste
- gas
- biomass
- fuel gas
- Prior art date
Links
Images
Classifications
-
- 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
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
-
- 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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Abstract
Description
本發明係關於一種生質能源發電系統及其運作方法,尤指一種可將生質物料轉化形成電力,以提供負載系統使用的生質能源發電系統及其運作方法。The invention relates to a biomass energy power generation system and an operation method thereof, in particular to a biomass energy power generation system and an operation method which can convert biomass materials into electricity to provide a load system.
20 世紀初,開發的行為在於追求能源高度的可用性與消費性,發明各式耗能的「主動式」設備與家電。20 世紀末則因為地球生態環境過度的破壞,節能的「被動式」設計再度為環保人士所重視。21 世紀初,面對「被動節能」的永續原則與「主動耗能」的舒適需求,新典範則是智慧地使用能源。區域、住所應該結合新的作法,以改善建築環境。At the beginning of the 20th century, the development behavior was to pursue a high degree of energy availability and consumption, inventing various types of energy-consuming "active" equipment and home appliances. At the end of the 20th century, because of the excessive destruction of the earth's ecological environment, energy-saving "passive" design was once again valued by environmentalists. At the beginning of the 21st century, facing the persistence principle of "passive energy saving" and the comfortable demand of "active energy consumption", the new paradigm is to use energy wisely. Areas and residences should incorporate new practices to improve the built environment.
畜牧業與農業是目前最不可或缺的產業,長久以來都佔有很重要的地位。舉以豬舍為例,目前在全台養頭數目約有550萬頭,而豬糞尿水加上清洗豬舍所產生的廢水,每日所產生的廢水量高達 20 多萬公噸,如此龐大數量的豬糞尿廢水,若直接排入溝渠或河川等水體,將直接衝擊水中的生物,破壞生態環境。Animal husbandry and agriculture are the most indispensable industries at present, and have occupied a very important position for a long time. Take the pig house as an example. At present, there are about 5.5 million heads in Taiwan. The amount of waste water generated by pig manure and urine plus the waste water from cleaning the pig house is as high as more than 200,000 metric tons per day. If the pig manure and urine wastewater is directly discharged into water bodies such as ditches or rivers, it will directly impact the organisms in the water and destroy the ecological environment.
因此,本發明提出一種生質能源發電系統及其運作方法,藉由替代性能源的開發結合發電機與運算控至,驅動「主動」的建築元件,以改善「被動」建築不足的效能與環境污染上的問題。Therefore, the present invention proposes a biomass energy power generation system and its operating method. By the development of alternative energy sources combined with generators and computing control, it drives “active” building elements to improve the performance and environment of “passive” building shortages. Problems with pollution.
有鑑於此,本發明之目的在於提出一種可透過生質物料轉化成電力,以供負載系統使用的生質能源發電系統及其運作方法,來達到節能減碳及能源自主的目標。In view of this, the purpose of the present invention is to propose a biomass energy power generation system that can be converted into electricity by biomass materials for use by a load system and an operation method thereof to achieve the goals of energy saving, carbon reduction and energy independence.
本發明之生質能源發電系統主要包含:至少一廢料排放設備,用以排放一廢料,且該廢料的PH值介於6-8之間;一燃料氣體生產系統,與該廢料排放設備連接,該燃料氣體生產系統產生一燃料氣體,包含:一廢料分離裝置;一厭氧醱酵裝置,與該廢料分離裝置連接;一氣體淨化裝置,與該厭氧醱酵裝置連接;以及一氣體儲存裝置,與該氣體淨化裝置連接。一氣體發電裝置,與該燃料氣體生產系統連接;一電力儲存裝置,與該氣體發電裝置連接;一電力控制裝置,與該電力儲存裝置和該氣體發電裝置連接;以及一負載系統,與該電力控制裝置連接。The biomass energy power generation system of the present invention mainly includes: at least one waste discharge device for discharging a waste, and the PH value of the waste is between 6-8; a fuel gas production system is connected to the waste discharge device, The fuel gas production system generates a fuel gas, including: a waste separation device; an anaerobic fermentation device connected to the waste separation device; a gas purification device connected to the anaerobic fermentation device; and a gas storage device , Connected to the gas purification device. A gas power generation device connected to the fuel gas production system; an electric power storage device connected to the gas power generation device; an electric power control device connected to the power storage device and the gas power generation device; and a load system connected to the electric power The control device is connected.
此外,本發明更提出一種生質能源發電系統的運作方法,包含以下步驟:(A)一廢料排放設備排放一廢料,且該廢料的PH值介於6-8之間;(B)一廢料分離裝置分離該廢料而形成一固體廢料和一液體廢料;(C)一厭氧醱酵裝置對該固體廢料進行厭氧醱酵反應以產生一生質氣體;(D)一氣體淨化裝置對該厭氧醱酵反應所產生的該生質氣體進行分離及純化處理,以形成一燃料氣體;以及(E)一氣體發電裝置透過該燃料氣體產生電力,並供給該電力至一負載系統。In addition, the present invention further proposes an operation method of a biomass energy power generation system, which includes the following steps: (A) a waste discharge device discharges a waste, and the PH value of the waste is between 6-8; (B) a waste The separation device separates the waste material to form a solid waste material and a liquid waste material; (C) an anaerobic fermentation enzyme device performs an anaerobic fermentation reaction on the solid waste material to produce a biomass gas; (D) a gas purification device The biomass gas produced by the oxygen fermentation reaction is separated and purified to form a fuel gas; and (E) a gas power generation device generates electricity through the fuel gas and supplies the electricity to a load system.
以上對本發明的簡述,目的在於對本發明之數種面向和技術特徵作一基本說明。發明簡述並非對本發明的詳細表述,因此其目的不在特別列舉本發明的關鍵性或重要元件,也不是用來界定本發明的範圍,僅為以簡明的方式呈現本發明的數種概念而已。The above brief description of the present invention aims to provide a basic description of several aspects and technical features of the present invention. The brief description of the invention is not a detailed description of the invention, so its purpose is not to specifically list the key or important elements of the invention, nor to define the scope of the invention, but to present several concepts of the invention in a concise manner.
為能瞭解本發明的技術特徵及實用功效,並可依照說明書的內容來實施,茲進一步以如圖式所示的較佳實施例,詳細說明如後:In order to understand the technical features and practical effects of the present invention, and to implement it in accordance with the contents of the specification, the preferred embodiments as shown in the drawings are further described in detail below:
本發明是一種可應用於畜牧業或農業的發電系統,可將大量的生質物料(如動物排泄物、農作物殘渣及廚餘等)轉化為電力,同時結合其他的再生能源,以達到節能減碳以及能源自主的目標。The invention is a power generation system applicable to animal husbandry or agriculture, which can convert a large amount of biomass materials (such as animal wastes, crop residues and kitchen waste, etc.) into electricity, while combining with other renewable energy sources to achieve energy saving and reduction The goal of carbon and energy independence.
首先,請參考第一圖,其為本發明較佳實施例之生質能源發電系統示意圖。如第一圖所示,本發明之生質能源發電系統1主要包含:一廢料排放設備10,用以排放一廢料,且該廢料的PH值介於6-8之間;一燃料氣體生產系統20,與該廢料排放設備10連接,該燃料氣體生產系統20產生一燃料氣體;一氣體發電裝置30,與該燃料氣體生產系統20連接;一電力儲存裝置40,與該氣體發電裝置30連接;一電力控制裝置50,與該電力儲存裝置40和該氣體發電裝置30連接;以及一負載系統60,與該電力控制裝置50連接。First, please refer to the first figure, which is a schematic diagram of a biomass energy power generation system according to a preferred embodiment of the present invention. As shown in the first figure, the biomass energy
具體而言,該廢料排放設備10可以是畜牧業的豬場、雞舍或馬廄等的排放設備,也可以是農業的穀倉、稻場或溫室等,抑或是一般的工業工廠。因此,該廢料排放設備10所排放出的廢料可能是人工基質,如葡萄糖、木糖、蔗糖、麥芽糖、澱粉或其組合;或是生質物料,如動物排泄物、農作物殘渣、廢水、廚餘或其組合。值得注意的是,不論是人工基質或生質物料,該些廢料的PH值皆須控制在6-8之間,才可產生較多的生質(燃料)氣體(可同時參照第二圖),以利於後續電力的生產。Specifically, the
而與該廢料排放設備10連接的燃料氣體生產系統20則負責將前述之廢料轉化成燃料氣體,並將該燃料氣體傳送至氣體發電裝置30以產生電力。其中,該燃料氣體生產系統20包含:一廢料分離裝置22;一厭氧醱酵裝置24,與該廢料分離裝置22連接;一氣體淨化裝置26,與該厭氧醱酵裝置24連接;以及一氣體儲存裝置28,與該氣體淨化裝置26連接。The fuel
具體而言,該廢料分離裝置22更包含一固液分離器222,用以分離前述之廢料;以及一收集處理器224,與該固液分離器222連接,該收集處理器224可收集該固液分離器222分離後的固體。該些經收集後的固體廢料則會透過厭氧醱酵裝置26\4進行厭氧醱酵反應以產生一生質氣體;最後,再藉由氣體淨化裝置26將該生質氣體進行分離、純化以及脫硫等步驟,形成如氫氣(H
2)或甲烷(CH
4)等燃料氣體,並透過氣體儲存裝置28加以儲存。
Specifically, the
而經由固液分離器222分離的液體則可透過與廢料分離裝置22(固液分離器222)連接的一濾沼槽223進行回收,並透過攪拌、過濾、濃縮以及分離等步驟製備有機複合液肥,可作為農作物及花卉等植物液肥使用。The liquid separated by the solid-
該氧醱酵反應裝置24還可包含有一醣化反應槽及設置於其內部的攪拌裝置(圖未示)、一營養鹽反應槽及設置於其內部的攪拌裝置(圖未示)、一混和槽及設置於其內部的攪拌裝置(圖未示),以及一醱酵反應槽(圖未示)。其中,醣化反應槽與營養鹽反應槽連通混合槽,並可將前述之固體廢料與營養鹽注入混合槽中攪拌混合;而混合槽連通醱酵反應槽,該醱酵反應槽可透過厭氧醱酵反應產生生質氣體。The oxo-
其中,醱酵反應槽主要是利用厭氧菌進行厭氧醱酵反應產生生質氣體,該醱酵反應槽可以是連續式攪拌反應器(Continuous-Stirred Tank Reactor, CSTR)、厭氧序批式反應器(Anaerobic Sequencing Batch Reactor, ASBR)、厭氧折流反應器(Anaerobic Baffled Bioreactor, ABR)、擔體誘發式顆粒污泥床(Carrier-Induced Granular Sludge Bed, CIGSB)、上流式厭氧污泥床(Up-flow Anaerobic Sludge Blanket, UASB)、膨脹式顆粒污泥床(Expended Granular Sludge Bed, EGSB)或攪拌式顆粒污泥床(Agitated Granular Sludge Bed, AGSB)。Among them, the fermentation reaction tank mainly uses anaerobic bacteria to perform anaerobic fermentation reaction to generate biomass gas. The fermentation reaction tank may be a continuous-stirred tank reactor (CSTR), anaerobic sequential batch type Reactor (Anaerobic Sequencing Batch Reactor, ASBR), Anaerobic Baffled Bioreactor (ABR), Carrier-Induced Granular Sludge Bed (CIGSB), Upflow Anaerobic Sludge Bed (Up-flow Anaerobic Sludge Blanket, UASB), Expanded Granular Sludge Bed (EGSB) or Agitated Granular Sludge Bed (AGSB).
由廢料轉化為燃料氣體的過程中,轉化的方式、廢料中硫化氫的濃度以及環境地控制條件(如溫度、濕度或壓力)等,皆會影響燃料氣體的生產效率。以下將對本發明中,廢料轉化的具體步驟作進一步的說明。In the process of converting waste into fuel gas, the conversion method, the concentration of hydrogen sulfide in the waste, and the environmental control conditions (such as temperature, humidity, or pressure) will affect the production efficiency of fuel gas. The specific steps of waste conversion in the present invention will be further described below.
首先,經由廢料排放設備10所排放的廢料會經由添加有脫水乾燥劑的廢料分離裝置22,以降低廢料的含水率;同時並控制該廢料的PH值介於6-8之間,以提高後續單位氣體的燃燒熱值。再者,將該些經脫水後的廢料放置於厭氧醱酵反應裝置24中以產生生質氣體(沼氣);其中,該厭氧醱酵反應裝置24的溫度應控制在40-70°C之間(較好的是50°C)、濕度控制在75-90%之間(較好的是80%),且醱酵的時間約為20-40日。而經由厭氧醱酵反應裝置24產生的生質氣體,會進入氣體淨化裝置26,並利用常溫的再生脫硫劑(如氧化鐵)去除生質氣體中的硫化氫(H
2S)氣體,以形成後續發電使用的燃料氣體。最後,再透過氣體儲存裝置28將該些燃料氣體壓縮儲存,且該氣體儲存裝置28還可包含一可控制壓力的閥門,調節從氣體儲存裝置28進入氣體發電裝置中燃料氣體的壓力,以維持氣體發電裝置30穩態運行。
First, the waste discharged through the
而透過前述之燃料氣體所生產系統生產的燃料氣體(如氫氣或甲烷)會進入氣體發電裝置30中產生電力。其中,該氣體發電裝置30為燃料電池發電裝置。燃料電池發電裝置在產生電力的過程中,主要透過氧氣或其他氧化劑進行氧化還原反應,將燃料氣體中的化學能轉換成電能的發電裝置,燃料電池相較於於原電池,其優點在於透過穩定地供應氧和燃料氣體,可持續不間斷的提供穩定電力直至燃料耗盡。The fuel gas (such as hydrogen or methane) produced by the aforementioned fuel gas production system will enter the gas
另一方面,燃料電池發電後會產生水與熱,基於使用不同的燃料,有可能產生極少量二氧化碳和其他物質,對環境的污染低於原電池或化石燃料發電廠,其中,燃料電池發電裝置的能量效率通常介於40-60%之間;若將發電後所產生廢熱回收使用,其裝置的能量效率更可達85-90%。因此,本發明之氣體發電裝置30還可與一熱能回收裝置80連接,該熱能回收裝置80可回收氣體發電裝置30燃燒發電後所產生的熱能,以提高發電的能量效率。On the other hand, fuel cells will generate water and heat after power generation. Based on the use of different fuels, it is possible to produce a very small amount of carbon dioxide and other substances. The pollution to the environment is lower than that of primary batteries or fossil fuel power plants. Among them, the fuel cell power plant The energy efficiency is usually between 40-60%; if the waste heat generated after power generation is recycled, the energy efficiency of its device can reach 85-90%. Therefore, the gas
氣體發電裝置30所產生的電力可直接經由電力控制裝置50的控制,分配到該至少一廢料排放設備10(亦可為本發明之負載系統60)中作使用;而多餘的電力則可透過電力儲存裝置40,且該電力儲存裝置40亦可作為該至少一廢料排放設備10的電力來源,藉此達到能源自主的目的。更進一步而言,該電力儲存裝置40還與至少一再生能源發電裝置70連接,並將該至少一再生能源發電裝置70所產生的電力儲存於電力儲存裝置40中。其中,該至少一再生能源發電裝置70可以是風力發電裝置、水力發電裝置、太陽能發電裝置或其組合。The power generated by the gas
而本發明之電力控制裝置50還可與一市電系統90並聯連接,以備於緊急情況發生或燃料氣體供應不足時,生質能源發電系統1可將負載系統60或至少一廢料排放設備10的供電來源自動切換至市電系統90,直至氣體發電裝置30的電力輸出正常為止,藉此提高本生質能源發電系統1電力傳輸的穩定度。The
另外,請同時參考第三圖,其為本發明較佳實施例之生質能源發電系統的運作方法流程圖。如第三圖所示,本發明所提出之生質能源發電系統1的運作方法包含以下步驟:(A)至少一廢料排放設備10排放一廢料,且該廢料的PH值介於6-8之間;(B)一廢料分離裝置22分離該廢料而形成一固體廢料和一液體廢料;(C)一厭氧醱酵裝置24對該固體廢料進行厭氧醱酵反應以產生一生質氣體;(D)一氣體淨化裝置26對該厭氧醱酵反應所產生的該生質氣體進行分離及純化處理,以形成一燃料氣體;以及(E)一氣體發電裝置30透過該燃料氣體產生電力,並供給該電力至一負載系統60。In addition, please also refer to the third figure, which is a flowchart of the operation method of the biomass energy power generation system according to the preferred embodiment of the present invention. As shown in the third figure, the operation method of the biomass energy
首先,在步驟(A)中,廢料排放設備10可以是畜牧業的豬場、雞舍或馬廄等的排放設備,也可以是農業的穀倉、稻場或溫室等,抑或是一般的工業工廠。因此,該廢料排放設備10所排放出的廢料可能是人工基質,如葡萄糖、木糖、蔗糖、麥芽糖、澱粉或其組合;或是生質物料,如動物排泄物、農作物殘渣、廢水、廚餘或其組合。First, in step (A), the
再者,在步驟(B)中,經廢料分離裝置22分離後所產生的固體廢料會被送至厭氧醱酵裝置24中以產生生質氣體;而液體廢料則可透過與廢料分離裝置連接的濾沼槽223進行攪拌、過濾、濃縮以及分離等步驟,以製備有機複合液肥。Furthermore, in step (B), the solid waste generated after being separated by the
接續,在步驟(C)中,厭氧醱酵裝置24會對該些固體廢料進行厭氧醱酵反應以產生生質氣體,在厭氧發酵的過程中環境的溫度、濕度和壓力,以及固體廢料的酸鹼值皆會影響生質氣體的產量,而本實施例之環境溫度控制在40-70°C、環境濕度控制在75-90%、固體廢料的酸鹼值控制在6-8,並經由一定的醱酵時間始可產出最大量的生質氣體。Next, in step (C), the
而在步驟(D)中,須將前述之生質氣體輸送進入氣體淨化裝置26進行純化處理,其中生質氣體純化的方法主要可分為:乾式氧化法 (Physical Absorption)、液體吸收法(Liquid Absorption)以及生物脫硫法(Bio-desulfurization)。In step (D), the above-mentioned biomass gas must be sent to the
前述之乾式氧化法包含:固體吸收法,使用顆粒狀的氧化鐵、石灰以批次方式處理吸收硫化氫;以及導入空氣與氧氣至生質氣體中,使得生質氣體中的硫化氫與氧氣結合形成水以及固態硫,以除去氣體中的硫化氫。前述之液體吸收法包含:物理高壓吸收法,將生質氣體與水壓縮(60-70kg/cm 2),使得二氧化碳與硫化氫溶於水中;物理低壓吸收法,將生質氣體與鹼性溶液(如氫氧化鈉)結合,吸收二氧化碳與硫化氫;以及化學吸收法,將氯化鐵(FeCl 3)直接添加至生質氣體以吸收硫化氫。而前述之生物脫硫法則包含:生物洗滌槽(Bioscrubber)、生物濾床(Biofilter)以及生物滴濾塔(Biotrickling)。 The aforementioned dry oxidation method includes: solid absorption method, using granular iron oxide and lime to process and absorb hydrogen sulfide in batch mode; and introducing air and oxygen into the biomass gas, so that the hydrogen sulfide in the biomass gas is combined with oxygen Water and solid sulfur are formed to remove hydrogen sulfide from the gas. The aforementioned liquid absorption method includes: physical high-pressure absorption method, which compresses biomass gas and water (60-70kg/cm 2 ) to make carbon dioxide and hydrogen sulfide dissolve in water; physical low-pressure absorption method, which combines biomass gas and alkaline solution (Such as sodium hydroxide) combine to absorb carbon dioxide and hydrogen sulfide; and chemical absorption method, add ferric chloride (FeCl 3 ) directly to the biomass gas to absorb hydrogen sulfide. The aforementioned biological desulfurization method includes: a biological scrubber (Bioscrubber), a biological filter bed (Biofilter) and a biological trickling filter tower (Biotrickling).
最後,在步驟(E)中,氣體發電裝置30透過該燃料氣體產生電力,並供給該電力至一負載系統60。其中,該氣體發電裝置30為燃料電池發電裝置;該負載系統60可以是外部負載,也可以是前述之廢料排放設備10,以達到綠化環境以及能源自主的目標。Finally, in step (E), the gas
惟以上所述者,僅為本發明之較佳實施例而已,當不能以此限定本發明實施之範圍,即依本發明申請專利範圍及說明內容所作之簡單變化與修飾,皆仍屬本發明涵蓋之範圍內。However, the above are only preferred embodiments of the present invention, and the scope of implementation of the present invention cannot be limited by this, that is, simple changes and modifications made according to the patent application scope and description of the present invention are still within the present invention. Covered.
1:生質能源發電系統1: Biomass power generation system
10:廢料排放設備10: Waste discharge equipment
20:燃料氣體生產系統20: Fuel gas production system
22:廢料分離裝置22: Waste separation device
222:固液分離器222: solid-liquid separator
223:濾沼槽223: Biogas tank
224:收集處理器224: Collect processor
24:厭氧醱酵裝置24: Anaerobic fermentation equipment
26:氣體淨化裝置26: Gas purification device
28:氣體儲存裝置28: Gas storage device
30:氣體發電裝置30: Gas power plant
40:電力儲存裝置40: Power storage device
50:電力控制裝置50: Power control device
60:負載系統60: load system
70:再生能源發電裝置70: Renewable energy power plant
80:熱能回收裝置80: thermal energy recovery device
90:市電系統90: Mains system
A-E:步驟A-E: Step
第一圖為本發明較佳實施例之生質能源發電系統示意圖。The first figure is a schematic diagram of a biomass energy power generation system according to a preferred embodiment of the present invention.
第二圖為本發明較佳實施例之燃料氣體產率曲線圖。The second graph is a fuel gas yield curve of a preferred embodiment of the present invention.
第三圖為本發明較佳實施例之生質能源發電系統的運作方法流程圖。The third figure is a flowchart of the operation method of the biomass energy power generation system according to the preferred embodiment of the present invention.
1:生質能源發電系統 1: Biomass power generation system
10:廢料排放設備 10: Waste discharge equipment
20:燃料氣體生產系統 20: Fuel gas production system
22:廢料分離裝置 22: Waste separation device
222:固液分離器 222: solid-liquid separator
223:濾沼槽 223: Biogas tank
224:收集處理器 224: Collect processor
24:厭氧醱酵裝置 24: Anaerobic fermentation equipment
26:氣體淨化裝置 26: Gas purification device
28:氣體儲存裝置 28: Gas storage device
30:氣體發電裝置 30: Gas power plant
40:電力儲存裝置 40: Power storage device
50:電力控制裝置 50: Power control device
60:負載系統 60: load system
70:再生能源發電裝置 70: Renewable energy power plant
80:熱能回收裝置 80: thermal energy recovery device
90:市電系統 90: Mains system
Claims (10)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
TW108100122A TWI690497B (en) | 2019-01-02 | 2019-01-02 | A power system of biofuel and the operating method thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
TW108100122A TWI690497B (en) | 2019-01-02 | 2019-01-02 | A power system of biofuel and the operating method thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
TWI690497B true TWI690497B (en) | 2020-04-11 |
TW202026252A TW202026252A (en) | 2020-07-16 |
Family
ID=71134317
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
TW108100122A TWI690497B (en) | 2019-01-02 | 2019-01-02 | A power system of biofuel and the operating method thereof |
Country Status (1)
Country | Link |
---|---|
TW (1) | TWI690497B (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TWI755789B (en) * | 2020-07-17 | 2022-02-21 | 謝永富 | Livestock sewage waste multi-level separation and reuse treatment system |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TWM480597U (en) * | 2014-01-06 | 2014-06-21 | Univ Feng Chia | Composite renewable energy supply system |
TW201602017A (en) * | 2014-07-15 | 2016-01-16 | Univ Feng Chia | Device for high-efficiency biological hydrogen and methane production |
TWM577017U (en) * | 2019-01-02 | 2019-04-21 | 逢甲大學 | Biomass energy power generation system |
-
2019
- 2019-01-02 TW TW108100122A patent/TWI690497B/en active
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TWM480597U (en) * | 2014-01-06 | 2014-06-21 | Univ Feng Chia | Composite renewable energy supply system |
TW201602017A (en) * | 2014-07-15 | 2016-01-16 | Univ Feng Chia | Device for high-efficiency biological hydrogen and methane production |
TWM577017U (en) * | 2019-01-02 | 2019-04-21 | 逢甲大學 | Biomass energy power generation system |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TWI755789B (en) * | 2020-07-17 | 2022-02-21 | 謝永富 | Livestock sewage waste multi-level separation and reuse treatment system |
Also Published As
Publication number | Publication date |
---|---|
TW202026252A (en) | 2020-07-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Xia et al. | Innovation in biological production and upgrading of methane and hydrogen for use as gaseous transport biofuel | |
Leng et al. | Bioenergy recovery from wastewater produced by hydrothermal processing biomass: Progress, challenges, and opportunities | |
Náthia-Neves et al. | Anaerobic digestion process: technological aspects and recent developments | |
Rocha-Meneses et al. | Second-generation bioethanol production: a review of strategies for waste valorisation. | |
Cavali et al. | Biochar and hydrochar in the context of anaerobic digestion for a circular approach: An overview | |
Kumar et al. | Efficiency of microbial fuel cells in the treatment and energy recovery from food wastes: trends and applications-a review | |
Varanasi et al. | Improvement of energy recovery from water hyacinth by using integrated system | |
Yu et al. | Production and utilization of methane biogas as renewable fuel | |
CN1769220A (en) | Marsh gas production technology using kitchen residue, straw, stock and fowl dejecta and active mud as material | |
CN103708693B (en) | A kind of municipal sewage treatment produce digestion system and the method for mud | |
CN203883489U (en) | Compound regenerative energy supply system | |
Song et al. | Recent advancements in strategies to improve anaerobic digestion of perennial energy grasses for enhanced methane production | |
Ning et al. | Emerging bioelectrochemical technologies for biogas production and upgrading in cascading circular bioenergy systems | |
Patil et al. | Anaerobic co-digestion of water hyacinth with primary sludge | |
TWI690497B (en) | A power system of biofuel and the operating method thereof | |
Noraini et al. | Factors affecting production of biogas from organic solid waste via anaerobic digestion process: A review | |
CN110078330A (en) | A kind of cold district oxygen-enriched combusting marsh gas power generation engineering system | |
CN107964552B (en) | Method for improving methane synthesis efficiency by coupling anaerobic digestion with MFC | |
Pandit et al. | Agricultural waste and wastewater as feedstock for bioelectricity generation using microbial fuel cells: recent advances. Fermentation. 2021; 7 (3): 169 | |
JP2011240238A (en) | Anaerobic bioreactor | |
TWM577017U (en) | Biomass energy power generation system | |
CN111484219A (en) | System and method for treating sludge through two-phase anaerobic digestion | |
CN216273829U (en) | Urban sludge treatment fertilizer making system based on pyrohydrolysis-ultrahigh temperature aerobic fermentation | |
Sawanon et al. | Grass as a high potential by-product: Buffalo grass to biogas and the increase of system performance and stability | |
KR101181834B1 (en) | Pre-thermal treatment of microalgae and high temperature and high efficiency hydrogen/methane fermentation process using waste heat of power-plant effluent gas |