JP2005068373A - Gasification method using self-catalysis of biomass - Google Patents
Gasification method using self-catalysis of biomass Download PDFInfo
- Publication number
- JP2005068373A JP2005068373A JP2003303533A JP2003303533A JP2005068373A JP 2005068373 A JP2005068373 A JP 2005068373A JP 2003303533 A JP2003303533 A JP 2003303533A JP 2003303533 A JP2003303533 A JP 2003303533A JP 2005068373 A JP2005068373 A JP 2005068373A
- Authority
- JP
- Japan
- Prior art keywords
- gasification
- biomass
- ash
- reaction
- gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Processing Of Solid Wastes (AREA)
- Industrial Gases (AREA)
Abstract
【課題】 原料バイオマス中の成分を有効利用し、外部から高価な触媒を添加することなく、低温側でガス化させて有用な合成ガスを高収率で得るバイオマスの効率的なガス化方法を提供する。
【解決手段】 バイオマス及びガス化剤をガス化炉に導入して合成ガスに転換させるバイオマスのガス化方法において、加熱条件下、ガス化反応系内にバイオマスから生成する灰分を存在させてガス化反応を行うことを特徴とするバイオマスのガス化法である。この方法は、バイオマスから副生し廃棄される灰分を有効利用するものであり、工業的実施に有用である。
【選択図】 なしPROBLEM TO BE SOLVED: To efficiently use biomass in raw material biomass and efficiently gasify biomass so as to obtain a useful synthesis gas in a high yield by gasifying on the low temperature side without adding an expensive catalyst from the outside. provide.
In a gasification method for biomass in which biomass and a gasifying agent are introduced into a gasification furnace and converted into synthesis gas, ash generated from biomass is present in the gasification reaction system in a gasification reaction under heating conditions. It is a biomass gasification method characterized by carrying out a reaction. This method effectively uses the ash that is produced as a by-product from biomass and is discarded, and is useful for industrial implementation.
[Selection figure] None
Description
本発明は、バイオマス原料を効率よくガス化させて有用ガスに転換させるバイオマスガス化法に関するものである。 The present invention relates to a biomass gasification method for efficiently gasifying a biomass material and converting it into a useful gas.
バイオマスは、唯一の再生可能な有機資源であり、貯蔵性、代替性を有し、再生時に大気中の二酸化炭素を固定するためカーボンニュートラルであり、莫大な賦存量を有する、等の特性がある。これらの特性を有するバイオマスは、エネルギー問題及び環境問題の軽減に寄与できる環境調和型のクリーンなエネルギー源として、今後大幅に導入することが提言されている。
このようなバイオマス、有機性廃棄物を含む有機物をガス化し、燃料ガスあるいは原料ガスを製造する技術については数多くの報告がある。これらのガス化技術の大きな課題は、副生するタールを如何に制御し得るかにあり、そのための手段としては、高温でガス化剤とともにガス化する方法、あるいは触媒の存在下で低温でガス化する方法などが試みられ、一部のものは既に実用化されている。前者に関しては、有機物を部分酸化した後、酸化反応と水性ガス化反応を併用してガス化する方法（例えば、特許文献１参照）、原料バイオマスの粒径及びガス化剤の供給比を限定するガス化法（例えば、特許文献２、３参照）及び底部に灰溜め部を形成したガス化炉を用いるバイオマスガス化法（例えば、特許文献４参照）などが提案されているが、これらの高温ガス化法は、多くのエネルギーを消費するにもかかわらず、タールの生成を抑制できないこと、高温操作に伴う装置の維持管理や操作の複雑さなどの諸問題があり、未だ満足できる方法は知られていない。
Biomass is the only renewable organic resource, has storability and substitutability, is carbon neutral because it fixes carbon dioxide in the atmosphere at the time of regeneration, has enormous potential, etc. . It has been proposed that biomass having these characteristics will be introduced significantly in the future as an environmentally harmonious clean energy source that can contribute to the reduction of energy and environmental problems.
There are many reports on the technology for producing fuel gas or raw material gas by gasifying organic substances including such biomass and organic waste. The major problem of these gasification technologies is how to control the tar produced as a by-product. As a means for this, a method of gasifying with a gasifying agent at a high temperature, or a gas at a low temperature in the presence of a catalyst. Some methods have already been put to practical use. Regarding the former, after partially oxidizing the organic matter, the method of gasifying by using the oxidation reaction and the water gasification reaction together (for example, refer to Patent Document 1), the particle size of the raw material biomass and the supply ratio of the gasifying agent are limited. Gasification methods (for example, see Patent Documents 2 and 3) and biomass gasification methods (for example, see Patent Document 4) using a gasification furnace in which an ash reservoir is formed at the bottom have been proposed. The gasification method consumes a lot of energy, but has problems such as the inability to suppress tar formation, equipment maintenance and operation complexity associated with high-temperature operation, and a method that is still satisfactory is known. It is not done.
また、触媒を用いる後者に関しては、セリウム酸化物担体の表面上にロジウム、ルテニウム、パラジウムまたは白金を担持させた触媒を用いて、４００〜１０００℃の低温側でガス化させる方法（例えば、特許文献５参照）、熱媒体機能を有する粘土からなるガス化促進剤を原料と流動接触させてガス化する方法（例えば、特許文献６参照）などが提案されている。これらの触媒を用いるガス化は、反応（ガス化）温度を低温側にシフトさせることができるためエネルギー的には有利であるが、金属系触媒は高価であり、また原料となる各種有機性物には灰分、硫黄及び燐等が含まれていることから、触媒の被毒や耐性低下（失活）の発生などの問題がある。 As for the latter using a catalyst, a method of gasifying at a low temperature of 400 to 1000 ° C. using a catalyst in which rhodium, ruthenium, palladium or platinum is supported on the surface of a cerium oxide support (for example, patent document) 5), and a method of gasifying the gasification accelerator made of clay having a heat medium function by fluid contact with the raw material (for example, see Patent Document 6). Gasification using these catalysts is advantageous in terms of energy because the reaction (gasification) temperature can be shifted to a lower temperature side. However, metal catalysts are expensive and various organic substances as raw materials are used. Since ash, sulfur, phosphorus and the like are contained in the catalyst, there are problems such as poisoning of the catalyst and generation of reduced resistance (deactivation).
本発明は、従来技術の上記した実情に鑑みてなされたものである。すなわち、本発明の目的は、原料バイオマス中に含まれる成分を有効利用することにより、外部から高価な触媒を添加することなく、低温側でガス化させて有用な合成ガスを高収率で得られるバイオマスの効率的なガス化方法を提供することにある。 The present invention has been made in view of the above-described actual situation of the prior art. That is, the object of the present invention is to effectively use the components contained in the raw material biomass to obtain a useful synthesis gas in a high yield by gasifying on the low temperature side without adding an expensive catalyst from the outside. It is in providing the efficient gasification method of the biomass obtained.
本発明は、バイオマス及びガス化材をガス化炉に導入して合成ガスに転換させるバイオマスのガス化方法であって、加熱条件下、ガス化反応系内にバイオマスから生成する灰分を存在させてガス化反応を行うことを特徴とするバイオマスのガス化方法である。このガス化方法で生成する合成ガスは、水素及び一酸化炭素を主成分とする有用なガスであり、メタノール、ジメチルエーテル（ＤＭＥ）などの液体燃料を製造するための原料ガスであることが好ましい。 The present invention is a biomass gasification method in which biomass and a gasification material are introduced into a gasification furnace and converted into synthesis gas, and ash generated from biomass is present in the gasification reaction system under heating conditions. It is a biomass gasification method characterized by performing a gasification reaction. The synthesis gas produced by this gasification method is a useful gas mainly composed of hydrogen and carbon monoxide, and is preferably a raw material gas for producing a liquid fuel such as methanol and dimethyl ether (DME).
本発明は、原料バイオマスの自己触媒作用などを利用してバイオマスのガス化を行うものであり、外部から高価な金属系の触媒を用いることなく、低温でガス化反応を促進させることができるから、安価にかつ省エネルギーで、高効率に液体燃料の原料や都市ガスなどに利用される有用なガスに転換できるものである。
また、本発明は、従来より産業廃棄物として処理問題となっている原料バイオマスから副生する灰分等の廃棄物を触媒作用を行うガス化反応促進剤としてリサイクル使用できるものであって、廃棄する灰分残さ量を削減できること及び低温でガス化できることから、環境汚染を軽減し、省エネルギー化を図ることのできる有益な方法である。
The present invention performs biomass gasification using the autocatalytic action of raw material biomass and the like, and the gasification reaction can be promoted at a low temperature without using an expensive metal-based catalyst from the outside. It can be converted into a useful gas used for a raw material of liquid fuel, city gas, etc. at low cost and energy saving and with high efficiency.
Further, the present invention can be recycled as a gasification reaction accelerator that catalyzes waste such as ash produced as a by-product from raw material biomass, which has been a treatment problem as industrial waste, and is discarded. Since it is possible to reduce the amount of ash residue and gasify at low temperature, it is a useful method that can reduce environmental pollution and save energy.
本発明は、バイオマスを含む有機性原料をガス化剤存在下にガス化して有用な合成ガスに変換する際、加熱条件下、ガス化反応系内に、バイオマスから生成する灰分等をガス化反応の促進剤（触媒など）として存在させてガス化反応を効率的に進行させるものであり、その灰分は、バイオマスから生成する灰分等を有効利用するものである。 In the present invention, when an organic raw material containing biomass is gasified in the presence of a gasifying agent to convert it into useful synthesis gas, the ash generated from biomass is gasified in the gasification reaction system under heating conditions. It is present as an accelerator (catalyst, etc.) to efficiently promote the gasification reaction, and the ash content effectively utilizes the ash content generated from biomass.
本発明に原料として用いるバイオマスとしては、有機工業原料或いは燃料として利用される天然由来の生物資源であれば使用可能であって、例えば、木材、草本、農林水産物の廃棄物などが挙げられるが、なかでも、ガス化反応、燃焼などによりある程度以上の灰分を生成するライグラス、イナワラ等の草類やマツの樹皮などを用いることが好ましい。また、杉、ヒノキ、ユウカリ木材部などの灰分を殆ど生成しないバイオマスを用いる場合には、上記した灰分を生成する草類などを適宜混合して用いるか、予めバイオマスのガス化で生成した灰分を反応系内にリサイクルするか、または、各種バイオマスの燃焼などで得られた新たな灰分を添加するなどの方法により、ガス化反応系内に一定量以上の灰分を存在させてガス化反応を行うものである。 The biomass used as a raw material in the present invention can be used as long as it is a natural biological resource used as an organic industrial raw material or fuel, and examples thereof include wood, herbaceous, agricultural, forestry and fishery wastes. Among them, it is preferable to use grass such as ryegrass and rice straw and pine bark that generate a certain amount or more of ash by gasification reaction or combustion. In addition, when using biomass that hardly produces ash, such as cedar, cypress, and eucalyptus wood, the above-mentioned grasses that produce ash are used in an appropriate mixture, or the ash produced by biomass gasification in advance is used. Recycling into the reaction system or adding a new amount of ash obtained from combustion of various biomass, etc. to carry out the gasification reaction with a certain amount or more of ash present in the gasification reaction system Is.
また、ガス化剤としては、酸素または酸素含有ガスと水蒸気が用いられる。さらに、ガス化反応により生成する合成ガスは、ＣＯ及びＨ２を主な有用成分とし、メタンなどの炭化水素類を含む有用なガスであり、例えば、メタノールやジメチルエーテルなどの液体燃料の合成原料或いは都市ガス等の燃料ガスとして用いられる。 As the gasifying agent, oxygen or oxygen-containing gas and water vapor are used. Furthermore, the synthesis gas produced by the gasification reaction is a useful gas containing CO and H 2 as main useful components and containing hydrocarbons such as methane. For example, a synthesis raw material of liquid fuel such as methanol or dimethyl ether or Used as fuel gas such as city gas.
本発明において、ガス化反応に用いる灰分は、バイオマスから生成する灰分原料中に含まれる灰分等の成分を、ガス化反応系内、特にガス化炉内を循環させるか、あるいは反応炉の任意の箇所、例えば、上部、中部或いは底部に浮遊または固定させ、ガス化の触媒として機能させてバイオマスのガス化を行うものである。そのガス化反応系に存在する灰分は、バイオマス原料及びガス化剤と良好に接触するようにガス化反応系内、特にガス化炉内に存在させることが好ましく、その灰分量としては、バイオマス原料に対し、０．５〜４０％の範囲であり、好ましくは５〜１０％である。これらの灰分は、後記する表３に見られるように、Ｓｉ、Ｋを主元素とし、その他にＦｅ、Ｃａ、Ｐ、Ｓ、Ａｌ、Ｍｇなどの多様な元素の酸化物からなるものである。 In the present invention, the ash used in the gasification reaction may be a component such as ash contained in the ash raw material produced from biomass, which is circulated in the gasification reaction system, particularly in the gasification furnace, or in any reactor Gasification of biomass is performed by floating or fixing at a location, for example, an upper portion, a middle portion, or a bottom portion, and functioning as a gasification catalyst. The ash present in the gasification reaction system is preferably present in the gasification reaction system, particularly in the gasification furnace, so as to make good contact with the biomass raw material and the gasifying agent. On the other hand, it is in the range of 0.5 to 40%, preferably 5 to 10%. These ash contents are composed of oxides of various elements such as Fe, Ca, P, S, Al, Mg, etc. in addition to Si and K as main elements, as can be seen in Table 3 to be described later.
ガス化反応を行う際、反応系内に存在する灰分が原料及びガス化剤と良く接触するように、反応系内にフィルターを設けることが好ましい。そのフィルターとしては、灰分を保持し、ガスと十分に接触する構造及び形状のものであればよく、その設置場所としては、ガス化炉内の上部、中部、底部のいずれの箇所でも良く、また、ガス化炉外のガス流路でも良い。また、ガス化反応温度は、灰分を存在させることで低温側にシフトさせることが可能であり、６５０〜１０００℃の範囲であるが、好ましくは６５０〜９００℃である。 When performing the gasification reaction, it is preferable to provide a filter in the reaction system so that the ash present in the reaction system is in good contact with the raw material and the gasifying agent. The filter may have any structure and shape that holds ash and is in sufficient contact with the gas, and may be installed at any of the top, middle, and bottom of the gasification furnace. Alternatively, a gas flow path outside the gasification furnace may be used. Further, the gasification reaction temperature can be shifted to a low temperature side by the presence of ash, and is in the range of 650 to 1000 ° C, preferably 650 to 900 ° C.
以下、図面を参照して本発明について具体的に説明する。
図１は、本発明のバイオマスのガス化反応に用いられる一例の噴流床型ガス化装置の概略構成図である。図１に示す装置に、前処理してある程度乾燥させた後、１ｍｍ程度に粉砕したバイオマス、ガス化剤の酸素及び水蒸気を、それぞれ常圧のガス化炉（反応管）に送り込むと、そのガス化炉内では、酸素により原料バイオマスの一部が燃焼し、８００〜１１００℃の高温に達してガス化反応に必要な熱を発生させ、残りのバイオマスは水蒸気でガス化されて、ＣＯ及びＨ２を主な有用成分とする生成ガスを得ることができる。
Hereinafter, the present invention will be specifically described with reference to the drawings.
FIG. 1 is a schematic configuration diagram of an example of a spouted bed type gasifier used in a biomass gasification reaction of the present invention. When the biomass shown in FIG. 1 is pretreated and dried to some extent and then pulverized to about 1 mm, gasification agent oxygen and water vapor are fed into a gasifier (reaction tube) at normal pressure, the gas In the gasification furnace, a part of the raw material biomass is burned by oxygen, reaches a high temperature of 800 to 1100 ° C. and generates heat necessary for the gasification reaction, and the remaining biomass is gasified with steam, and CO and H A product gas having 2 as a main useful component can be obtained.
図１のガス化装置を用いて、２種類のバイオマス原料、すなわち、スギ（木材部分）とイタリアンライグラス（地上部全草）のガス化を行った。用いた原料バイオマスの性状として、表１にはスギ、また表２にはイタリアンライグラスのそれぞれの元素分析値を示す。
スギ（木材部）は、炭素、水素、酸素の３元素で構成され、イオウ、灰分の含有率が低く、窒素は殆ど含まれていないのに対し、イタリアンライグラス（地上部全草）は灰分の含有率が高く、また窒素、イオウも微量含まれている。
Cedar (wood) is composed of three elements, carbon, hydrogen, and oxygen, and the content of sulfur and ash is low and contains almost no nitrogen, whereas Italian ryegrass (overall grass) has ash content. The content is high and also contains a small amount of nitrogen and sulfur.
次に、イタリアンライグラスの灰分の分析結果（酸化物表示）を表３に示す。
スギ及びライグラスのガス化
ガス化反応は、反応温度を７００〜１０００℃の範囲とし、ガス化剤（酸素と水蒸気）は、［Ｏ２］／［Ｃ］比を０〜０．４５、［Ｈ２Ｏ］／［Ｃ］比を０．５〜１５で変化させ、２つのパラメータを組み合わせた種々の条件でガス化を行った。
（［Ｏ２］／［Ｃ］比＝原料バイオマス中の炭素のモル数に対し、添加した酸素のモル数比、実際には１分当りのバイオマス投入量（ｇ／ｍｉｎ）に含まれる炭素のモル数を分母とし、１分当りの酸素流量（ｃｃ／ｍｉｎ）を分子として［Ｏ２］／［Ｃ］比とした。［Ｈ２Ｏ］／［Ｃ］比についても同様である。）
スギについては、スギ単独の場合と、スギにライグラスの灰分を添加した混合物の場合の２種類をガス化した。ライグラスの灰分は、ライグラスをガス化し、反応後に得られた残さを回収したものを用いた。
Gasification of cedar and ryegrass The gasification reaction takes a reaction temperature in the range of 700 to 1000 ° C., and the gasifying agent (oxygen and water vapor) has an [O 2 ] / [C] ratio of 0 to 0.45, [H The 2 O] / [C] ratio was varied from 0.5 to 15, and gasification was performed under various conditions combining two parameters.
([O 2 ] / [C] ratio = ratio of moles of oxygen added to moles of carbon in raw biomass, actually the amount of carbon contained in biomass input (g / min) per minute) The number of moles is the denominator, the oxygen flow rate per minute (cc / min) is the numerator, and the [O 2 ] / [C] ratio is used, and the same applies to the [H 2 O] / [C] ratio.)
As for the cedar, two kinds of cedar alone and a mixture obtained by adding ryegrass ash to the cedar were gasified. The ash content of ryegrass was obtained by gasifying ryegrass and collecting the residue obtained after the reaction.
バイオマスガス化の一連の手順は、次のとおりである。
まず、ガス化炉を所定温度に設定し、加熱した。その後、反応管の上部と下部からそれぞれ窒素ガスを流し、安定したところで酸素と水（水蒸気）（いずれもガス化剤として使用）を設定量流した。次に、原料供給器（自動供給ができるよう設計製作）にバイオマス原料を入れ、秤量した後、外枠体に取り付け、この装置一式を反応管上部に取り付けた。次に、反応管及び原料供給器の準備が整った後、原料の供給を開始しガス化を行った。原料供給器に１回に供給する量は１２〜１５ｇ（原料の種類と粉砕状況に応じて異なる。）であり、１分当り０．６〜０．８ｇを反応管に供給した。
A series of procedures for biomass gasification is as follows.
First, the gasification furnace was set to a predetermined temperature and heated. Thereafter, nitrogen gas was allowed to flow from the upper part and the lower part of the reaction tube, respectively, and oxygen and water (water vapor) (both used as gasifying agents) were allowed to flow in a set amount when stable. Next, the biomass raw material was put into a raw material feeder (designed and manufactured so that automatic supply can be performed), weighed and then attached to the outer frame, and this set of devices was attached to the upper part of the reaction tube. Next, after the preparation of the reaction tube and the raw material supplier was completed, the raw material supply was started and gasification was performed. The amount supplied to the raw material supplier at one time was 12 to 15 g (depending on the type of raw material and the pulverization condition), and 0.6 to 0.8 g per minute was supplied to the reaction tube.
原料の供給開始と共に生成してくるガス留分は、反応管上部より誘導され、フィルター（セラミックフィルター設置）部分、冷却管部分、ドレイン瓶部分及びガスメータを順次通過して、最後はガスサンプリングバッグに収集される。ガス化に伴う生成物としては、ガス、固体残さ（チャーやスス、あるいは未反応の原料など）、タール及び水溶性化合物であった。ガスはガスメータで容量を量り、ガスサンプリングバッグ（テドラー製ガスバッグ）にて採集した。収集したガスの組成については、ＣＯ、ＣＯ２、Ｈ２、ＣＨ４及びＣ２＋の５種をＧＣで分析した。
固体残さはフィルター部分で回収し、またタールは冷却管をアセトン洗浄し、アセトン溶液として回収し、それぞれ重量をはかり、重量の多いものについては、元素分析を行った。水溶性化合物はドレイン瓶にて水とともに回収し、水溶液の重量とＴＯＣを測定した。
The gas fraction generated at the start of the supply of the raw material is guided from the upper part of the reaction tube, passes sequentially through the filter (ceramic filter installation) part, the cooling pipe part, the drain bottle part and the gas meter, and finally into the gas sampling bag. Collected. Products resulting from gasification were gas, solid residue (such as char and soot, or unreacted raw materials), tar, and water-soluble compounds. The gas was measured with a gas meter and collected with a gas sampling bag (Tedlar gas bag). Regarding the composition of the collected gas, five kinds of CO, CO 2 , H 2 , CH 4 and C 2 + were analyzed by GC.
The solid residue was collected at the filter portion, and tar was washed in the cooling tube with acetone and collected as an acetone solution. Each of these was weighed, and the heavy one was subjected to elemental analysis. The water-soluble compound was collected together with water in a drain bottle, and the weight and TOC of the aqueous solution were measured.
表４には、ガス化反応の結果をＲｕｎＡ〜Ｇとして示す。
表４中、［Ｏ２］／［Ｃ］比＝約０．１ ［Ｈ２Ｏ］／［Ｃ］比＝約１．５は、パラメータ探索により、良好な結果を示した条件に基づいて設定したものである。また、「Ｃ−ｒｅｃｏｖｅｒｙ ｉｎｔｏ ｇａｓ（ガス化率）」及び「Ｃ−ｒｅｃｏｖｅｒｙ」については、それぞれ次のように定義した。
Ｃ−ｒｅｃｏｖｅｒｙ ｉｎｔｏ ｇａｓ（ガス化率）＝
生成ガス中に含まれる炭素量（ＣＯ＋ＣＯ２＋ＣＨ４＋Ｃ２ガスのＣモル数）／
原料バイオマス中に含まれる炭素量（原料中のＣモル数）
Ｃ−ｒｅｃｏｖｅｒｙ ＝
（生成ガス＋固体残さ＋タール＋回収水溶液）中に含まれる炭素量（Ｃモル数）／
原料バイオマス中に含まれる炭素量（原料中のＣモル数）
Table 4 shows the results of the gasification reaction as RunA to G.
In Table 4, [O 2 ] / [C] ratio = about 0.1 [H 2 O] / [C] ratio = about 1.5 is set based on the conditions showing good results by parameter search. It is a thing. Further, “C-recovery into gas (gasification rate)” and “C-recovery” were defined as follows.
C-recovery into gas (gasification rate) =
The amount of carbon contained in the product gas (C + CO 2 + CH 4 + C moles of C 2 gas) /
Carbon content in raw material biomass (C moles in raw material)
C-recovery =
(Production gas + solid residue + tar + recovered aqueous solution) carbon content (C moles) /
Carbon content in raw material biomass (C moles in raw material)
反応温度７００〜１０００℃におけるスギのガス化結果を比較すると、７００℃におけるＣ−ｒｅｃｏｖｅｒｙ ｉｎｔｏ ｇａｓは０．５９と低く（ＲｕｎＡ）、温度の上昇とともに増加し、１０００℃では０．９程度になった。なお、従来の触媒を添加しない場合、ガス化の適正温度は９００〜１０００℃であることが知られている。
ＲｕｎＥは、スギ１２．７８０ｇにライグラス灰分１．０９３ｇ（灰分７．８重量％）の割合で添加し、またＲｕｎＦは、スギ１０．２１５ｇにライグラス灰分０．３５３ｇの割合で添加して、それぞれガス化を行った。ガス化条件は、ＲｕｎＥはＲｕｎＡ（７００℃）と、またＲｕｎＦはＲｕｎＣ（９００℃）とほぼ同じである。
その結果、ガス化条件がほぼ等しいにも係わらず、ガス化率（Ｃ−ｒｅｃｏｖｅｒｙ ｉｎｔｏ ｇａｓ）は、ＲｕｎＥにおいて０．７２とＲｕｎＡに比較して２２％、ＲｕｎＦにおいて０．９５とＲｕｎＣに比較して２５％増加している。このガス化の差は、ライグラス灰分の添加によるものと考えられる。また、灰分の添加により、ガス化温度を低温側へシフトさせることが可能である、あるいは同じ温度でガス化する場合は、ガス化率を増加させることができることが判明した。
Comparing the results of gasification of cedar at a reaction temperature of 700 to 1000 ° C., C-recovery into gas at 700 ° C. is as low as 0.59 (Run A), increases with increasing temperature, and becomes about 0.9 at 1000 ° C. It was. In addition, when not adding the conventional catalyst, it is known that the appropriate temperature of gasification is 900-1000 degreeC.
RunE is added at a rate of 1.093 g of ryegrass ash (ash content: 7.8 wt%) to 12.780 g of cedar, and RunF is added at a rate of 0.353 g of ryegrass ash to 10.215 g of cedar. Made. The gasification conditions are almost the same for Run E as Run A (700 ° C.) and Run F as Run C (900 ° C.).
As a result, the gasification rate (C-recovery into gas) was 0.72 for RunE, 22% compared to RunA, and 0.95 for RunF, even though the gasification conditions were almost equal. Increase by 25%. This difference in gasification is thought to be due to the addition of ryegrass ash. It has also been found that the gasification temperature can be shifted to a lower temperature side by adding ash, or the gasification rate can be increased when gasifying at the same temperature.
また、ライグラスの９００℃、［Ｏ２］／［Ｃ］比＝０．１１，［Ｈ２Ｏ］／［Ｃ］比＝２．３の条件（スギのＲｕｎＣに近い条件）でガス化した結果（ＲｕｎＧ）は、ガス化率はスギより若干高いが、生成ガス組成をみるとＣＯ及びＨ２の生成ガス中に占める比率は、同条件でスギから得られたガスのそれらに比べて低かった。
さらに、ライグラスのガス化後に得られた灰分をスギに添加してガス化すると（ＲｕｎＦ）、ガス化率が増加し、生成ガスもＣＯ及びＨ２の割合の高いメタノール等の液体燃料製造に適した組成となった。これはスギ単独、あるいはライグラス単独でガス化するよりも、灰分を含んだ原料を他種のバイオマスと混合してガス化することによりガス化率が増加する、という混合効果を示すもので、実際のガス化にあたっては、多種のバイオマスをそのまま分別、限定することなく、ガス化することができるという利点を有する。
これらの実験結果は、これまで廃棄物として処理が問題となっていた灰分を、ガス化触媒として有効利用できることを示すものである。
The result of gasification of ryegrass at 900 ° C., [O 2 ] / [C] ratio = 0.11, [H 2 O] / [C] ratio = 2.3 (a condition close to Sugi RunC) (RunG) has a gasification rate slightly higher than that of cedar, but the composition ratio of CO and H 2 in the product gas is lower than those of the gas obtained from cedar under the same conditions. .
Furthermore, when the ash obtained after gasification of ryegrass is added to cedar and gasified (RunF), the gasification rate increases and the product gas is also suitable for liquid fuel production such as methanol with a high proportion of CO and H 2 Composition. This shows the mixing effect that the gasification rate increases by mixing and gasifying raw material containing ash with other types of biomass, rather than gasifying with cedar alone or ryegrass alone. In the gasification, there is an advantage that various kinds of biomass can be gasified without being separated and limited as they are.
These experimental results show that ash, which has been a problem as a waste, can be effectively used as a gasification catalyst.
本発明のバイオマスのガス化方法は、産業廃棄物及び生活廃棄物とされている各種バイオマスを有用なガスに転換させる際、従来は廃棄処理されていた副生する灰分等を有効利用するものであるうえに、比較的低温で簡易にガス化反応を行うことができるから、工業的実施に有用である。 The biomass gasification method of the present invention effectively uses by-product ash that has been disposed of in the past when converting various types of biomass, which are industrial waste and domestic waste, to useful gas. In addition, since the gasification reaction can be easily performed at a relatively low temperature, it is useful for industrial implementation.
Claims (5)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2003303533A JP4085160B2 (en) | 2003-08-27 | 2003-08-27 | Gasification method using self-catalysis of biomass |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2003303533A JP4085160B2 (en) | 2003-08-27 | 2003-08-27 | Gasification method using self-catalysis of biomass |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2005068373A true JP2005068373A (en) | 2005-03-17 |
| JP4085160B2 JP4085160B2 (en) | 2008-05-14 |
Family
ID=34407499
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2003303533A Expired - Lifetime JP4085160B2 (en) | 2003-08-27 | 2003-08-27 | Gasification method using self-catalysis of biomass |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP4085160B2 (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008303377A (en) * | 2007-05-08 | 2008-12-18 | National Institute Of Advanced Industrial & Technology | Method for generating combustible gas and gasification reactor therefor |
| JP2009532483A (en) * | 2006-04-05 | 2009-09-10 | ウッドランド バイオフュールズ インコーポレイテッド | Method for converting biomass to ethanol via synthesis gas |
| JP2012255114A (en) * | 2011-06-10 | 2012-12-27 | Ihi Corp | System and method for producing gasified gas |
| JP2014105120A (en) * | 2012-11-26 | 2014-06-09 | National Institute Of Advanced Industrial & Technology | Methane reforming method and methane reforming catalyst used for the same |
| CN113462435A (en) * | 2021-06-25 | 2021-10-01 | 浙江工业大学 | Resource recycling catalytic utilization method for biomass gasification ash |
| CN119331652A (en) * | 2024-12-05 | 2025-01-21 | 宁夏大学 | A method for co-gasification of coal and biomass |
-
2003
- 2003-08-27 JP JP2003303533A patent/JP4085160B2/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009532483A (en) * | 2006-04-05 | 2009-09-10 | ウッドランド バイオフュールズ インコーポレイテッド | Method for converting biomass to ethanol via synthesis gas |
| JP2008303377A (en) * | 2007-05-08 | 2008-12-18 | National Institute Of Advanced Industrial & Technology | Method for generating combustible gas and gasification reactor therefor |
| JP2012255114A (en) * | 2011-06-10 | 2012-12-27 | Ihi Corp | System and method for producing gasified gas |
| JP2014105120A (en) * | 2012-11-26 | 2014-06-09 | National Institute Of Advanced Industrial & Technology | Methane reforming method and methane reforming catalyst used for the same |
| CN113462435A (en) * | 2021-06-25 | 2021-10-01 | 浙江工业大学 | Resource recycling catalytic utilization method for biomass gasification ash |
| CN119331652A (en) * | 2024-12-05 | 2025-01-21 | 宁夏大学 | A method for co-gasification of coal and biomass |
Also Published As
| Publication number | Publication date |
|---|---|
| JP4085160B2 (en) | 2008-05-14 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Asadullah et al. | Biomass gasification to hydrogen and syngas at low temperature: novel catalytic system using fluidized-bed reactor | |
| Wang et al. | Contemporary issues in thermal gasification of biomass and its application to electricity and fuel production | |
| AU2007275752B2 (en) | Controlling the synthesis gas composition of a steam methane reformer | |
| Ptasinski | Thermodynamic efficiency of biomass gasification and biofuels conversion | |
| Saxena et al. | Thermo-chemical routes for hydrogen rich gas from biomass: a review | |
| RU2544666C2 (en) | Regulation of synthesis-gas composition in installation of steam methane reforming | |
| Lv et al. | Steam co-gasification of different ratios of spirit-based distillers’ grains and anthracite coal to produce hydrogen-rich gas | |
| Luo et al. | Biomass gasification: an overview of technological barriers and socio-environmental impact | |
| Peres et al. | Application of biomass to hydrogen and syngas production | |
| AU2007275751B2 (en) | Operation of a steam methane reformer by direct feeding of steam rich producer gas from steam hydro-gasification | |
| Saghir et al. | Recent trends in gasification based waste-to-energy | |
| US20100132633A1 (en) | Biomass gasification reactor | |
| CN103497840B (en) | Method for comprehensively utilizing abandoned oil in coking industries | |
| Asadullah et al. | Role of catalyst and its fluidization in the catalytic gasification of biomass to syngas at low temperature | |
| Vallejo et al. | Valorization of municipal solid waste using hydrothermal carbonization and gasification: A review | |
| EP3029016B1 (en) | Method and system for acetylene (CH2) or ethylene (C2H4) production | |
| JP4085160B2 (en) | Gasification method using self-catalysis of biomass | |
| MX2009000701A (en) | Method and apparatus for steam hydro-gasification in a fluidized bed reactor. | |
| Iaquaniello et al. | Waste as a source of carbon for methanol production | |
| Marx | Experimental Investigation in Autothermal Chemical Looping Gasification | |
| Marie-Rose et al. | From biomass-rich residues into fuels and green chemicals via gasification and catalytic synthesis | |
| KR100519386B1 (en) | A method on manufatcturing of synthesis gas from paper sludge | |
| Al Arni | Thermochemical hydrogen production routes from biomass: gasification, reforming, and pyrolysis | |
| Hong | Application and Optimization of Thermochemical Conversion Methods for Energy Utilization of Forestry Waste | |
| Marie-Rose et al. | From biomass-rich residues into fuels and green chemicals via gasification and catalytic synthesis |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20050315 |
|
| A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20071022 |
|
| A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20071106 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20071225 |
|
| TRDD | Decision of grant or rejection written | ||
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20080122 |
|
| R150 | Certificate of patent or registration of utility model |
Ref document number: 4085160 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
| S533 | Written request for registration of change of name |
Free format text: JAPANESE INTERMEDIATE CODE: R313533 |
|
| R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |
|
| EXPY | Cancellation because of completion of term |