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JP2005179405A - Apparatus for feeding granular raw material for biomass conversion type gas producer - Google Patents

Apparatus for feeding granular raw material for biomass conversion type gas producer Download PDF

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JP2005179405A
JP2005179405A JP2003418816A JP2003418816A JP2005179405A JP 2005179405 A JP2005179405 A JP 2005179405A JP 2003418816 A JP2003418816 A JP 2003418816A JP 2003418816 A JP2003418816 A JP 2003418816A JP 2005179405 A JP2005179405 A JP 2005179405A
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raw material
screw conveyor
furnace
granular raw
pipe
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Yukimaru Shimizu
幸丸 清水
Yasunari Kamata
泰成 鎌田
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Mie TLO Co Ltd
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Mie TLO Co Ltd
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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
    • 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
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/141Feedstock
    • Y02P20/145Feedstock the feedstock being materials of biological origin
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/78Recycling of wood or furniture waste

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  • Processing Of Solid Wastes (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
  • Coke Industry (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide an apparatus for feeding a vegetable granular raw material for a biomass conversion type gas producer designed to prevent clogging of a charging pipe with the vegetable granular raw material such as wood flour, stably feed the vegetable granules into the furnace and thereby excellently safely and stably perform operation. <P>SOLUTION: The apparatus is composed as follows. The vegetable granular raw material is transported through a screw conveyor 12 arranged in the intermediate part of a granular raw material tank 11 and the charging pipe 13 into the interior of a biomass gas furnace while continuously applying a pressure to the vegetable granular raw material without causing clogging as indicated by a drawing. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、草木類などの植物燃料を原料として一酸化炭素や水素等の可燃性有用ガスを生成するバイオマス変換式のガス発生装置に関するものであり、特に微粉体形状の植物燃料の炉内への投入が安定して行えると共に、安全性が改善された、新規な構造のバイオマス変換式ガス発生装置に関するものである。   The present invention relates to a biomass conversion-type gas generator that generates flammable useful gas such as carbon monoxide and hydrogen using plant fuel such as vegetation as a raw material, and particularly into a plant fuel furnace in the form of fine powder. The present invention relates to a biomass conversion gas generator having a novel structure that can be stably charged and has improved safety.

従来から、木材加工業等で多量に発生する切粉、おが屑や削り屑,木片,間伐材等の木質系廃棄物の活用装置の一種として、バイオマスのガス化によるエネルギー利用技術の一つであるバイオマス変換式のガス発生装置が知られている。   Conventionally, it is one of the energy utilization technologies by gasification of biomass as a kind of utilization equipment of wood waste such as chips, sawdust and shavings, wood chips, thinned wood, etc. generated in large quantities in the wood processing industry etc. A biomass conversion type gas generator is known.

かかるガス発生装置は、例えば特許文献1に示されているように、竪型中空の炉体の下部に空気取入口を設けると共に、上壁を貫通して略鉛直方向に延びる投入パイプを配設して、炉体上方に設置した燃料タンクから投入パイプを通じて炉内に木粉等を供給せしめつつ、炉内に堆積した木粉等の最下部で熱分解後の木粉等を酸化燃焼させて、発生する熱により上方の木粉等を乾燥・熱分解せしめることにより熱分解ガスを生成するようになっている。また、炉内に堆積した木粉等の中〜下層の領域で発生した熱分解ガスは、堆積した木粉等中を通過することで冷却・濾過された後、炉体の上部に開口するガス吸引管を通じて吸引されることにより炉外に取り出されるようになっており、その後、サイクロン等の適当な浄化装置によってダストやタールの除去が行われることにより、清浄な可燃性の有用ガスとして利用に供されることとなる。   For example, as disclosed in Patent Document 1, such a gas generator is provided with an air inlet at the lower part of a vertical hollow furnace body and an input pipe that extends through the upper wall in a substantially vertical direction. Then, while supplying wood powder etc. into the furnace through the input pipe from the fuel tank installed above the furnace body, the pyrolyzed wood powder etc. is oxidized and burned at the bottom of the wood powder etc. accumulated in the furnace The wood powder or the like is dried and thermally decomposed by the generated heat to generate pyrolysis gas. In addition, the pyrolysis gas generated in the middle to lower layer of wood powder accumulated in the furnace is cooled and filtered by passing through the accumulated wood powder and the like, and then opened to the top of the furnace body It is designed to be taken out of the furnace by being sucked through the suction tube, and then removed as dust or tar by an appropriate purification device such as a cyclone, so that it can be used as a clean and combustible useful gas. Will be served.

実開平6−84109号公報Japanese Utility Model Publication No. 6-84109

さて、既知の技術によれば、炉体の上壁上には、燃料タンクが載置されて固設されている。この燃料タンクは中空円形又は中空円筒形の容器であって、燃料タンクの上方にはホッパが配設されており、このホッパの下端に形成された吐出口が、燃料タンクの燃料受口上に開口せしめられている。   According to a known technique, a fuel tank is placed and fixed on the upper wall of the furnace body. This fuel tank is a hollow circular or hollow cylindrical container. A hopper is disposed above the fuel tank, and a discharge port formed at the lower end of the hopper opens above the fuel receiving port of the fuel tank. I'm hurt.

そして、燃料となる木粉等がニューマチックコンベヤ等により、搬送パイプを通じて燃料タンクに供給されるようになっている。更に、燃料タンクに供給された木粉等を、必要に応じて、燃料タンク内に導き入れることが出来るようになっている。   And the wood powder etc. used as a fuel are supplied to a fuel tank through a conveyance pipe by a pneumatic conveyor or the like. Further, wood powder or the like supplied to the fuel tank can be introduced into the fuel tank as necessary.

ところが、従来構造のガス発生装置では、燃料タンクから供給される微粉粒体形状の木粉等の形状や水分量、締まり具合などの各種条件によって、木粉等の原料が投入パイプの途中で降下しなくなる棚つり現象などが発生し、円滑な供給が出来なくなる状況がしばしば発生した。このため、安定操業ができなくなる上に異常燃焼等の安全上の問題があった。   However, in conventional gas generators, raw materials such as wood powder fall in the middle of the input pipe depending on various conditions such as the shape of fine powder and wood powder supplied from the fuel tank, moisture content, and tightening conditions. There was often a situation where shelves could not be smoothly supplied due to the shelving phenomenon. For this reason, stable operation cannot be performed and there are safety problems such as abnormal combustion.

これに対し、本発明者らは、特許文献2に示すように、下方に拡開するようにテーパをつけた投入パイプ並びに投入パイプの上端から下方に向かって送りスクリューを配設し、木粉等を強制的に送り込む装置を考案した。これにより、詰まりが改善されたが、未だ十分ではなかった。   On the other hand, as shown in Patent Document 2, the present inventors arranged a feed pipe tapered so as to expand downward, a feed screw from the upper end of the feed pipe downward, and wood powder. I devised a device that forcibly feeds etc. This improved clogging, but it was not enough.

特願2002−287031号Japanese Patent Application No. 2002-287031

本発明の解決課題とするところは、投入パイプへの木粉等の植物性粉粒体原料の詰まりが防止されて、植物性粉粒体を炉内に安定して供給することができ、それによって、優れた安全性をもって安定して操業することが可能なバイオマス変換式ガス発生炉用の植物性粉粒体原料供給装置を提供することにある。   The problem to be solved by the present invention is that clogging of plant powder material such as wood powder into the input pipe is prevented, and the plant powder can be stably supplied into the furnace. Therefore, an object of the present invention is to provide a plant powder raw material supply device for a biomass conversion gas generator that can be stably operated with excellent safety.

本発明は、上記の課題を解決するためになされたもので、粉粒体原料タンクと投入パイプの中間部に配設されたスクリューコンベア(Screw conveyor)を介して、植物性粉粒体原料がバイオマスガス炉内に、詰まりを生ずることなく搬送されるように装置を構成することによって達成される。   The present invention has been made in order to solve the above-described problems, and the plant granular material is obtained via a screw conveyor (Screw conveyor) disposed between the granular material raw material tank and the input pipe. This is accomplished by configuring the apparatus to be transported into the biomass gas furnace without causing clogging.

具体的には、本発明の装置は、筒型の周壁部を備えた竪型中空の炉体上方に設置した粉粒体原料タンクから、木粉等の植物性粉粒体原料を、該炉体の上部を貫通して配設した投入パイプを通じて、該炉体の内部に供給しつつ、該炉体の内部で植物性粉粒体原料を熱分解せしめて発生ガスを炉外に吸引収集するようにしたバイオマス変換式ガス発生装置において、粉粒体原料タンクと投入パイプの中間部にスクリューコンベア(Screw conveyor)を配設し、該粉粒体原料タンクの原料排出口とスクリューコンベア(Screw conveyor)の原料受入口、及び、該スクリューコンベア(Screw conveyor)の原料排出口と投入パイプの上部開口部が、各々連結管により連結された植物性粉粒体原料供給装置にある。   Specifically, the apparatus of the present invention is configured to supply plant powder raw materials such as wood powder from a powder raw material tank installed above a vertical hollow furnace body having a cylindrical peripheral wall. While supplying to the inside of the furnace body through an input pipe arranged through the upper part of the body, the plant granular material is pyrolyzed inside the furnace body and the generated gas is sucked and collected outside the furnace body. In the biomass conversion type gas generator configured as described above, a screw conveyor (Screw conveyor) is arranged in the middle part of the granular material raw material tank and the input pipe, and the raw material discharge port of the granular material raw material tank and the screw conveyor (Screw conveyor) are arranged. ), And the raw material outlet of the screw conveyor (Screw conveyor) and the upper opening of the input pipe are connected to each other by a connecting pipe. That.

これにより、植物性粉粒体原料(以下、粉粒体原料と略記する)は、上記のスクリューコンベアから投入パイプに連続的に圧送され、投入パイプ内の粉粒体原料に常に下方への押圧力を負荷することによって、詰まりを防止すると共に、マテリアルシールとして(原料による密閉状態)路蓋の作用も有している。   As a result, the vegetable powder raw material (hereinafter abbreviated as powder raw material) is continuously pumped from the screw conveyor to the charging pipe and is always pushed downward into the powder raw material in the charging pipe. By applying the pressure, clogging is prevented, and the road cover also functions as a material seal (sealed state with raw materials).

本発明によって、バイオマス変換式ガス発生炉に粉粒体原料を安定して供給することができ、優れた安全性をもって安定して操業することが可能となり、省力化、安全性及び経済性に優れた装置を供給できるようになった。   According to the present invention, it is possible to stably supply powder raw materials to a biomass conversion gas generating furnace, and it is possible to stably operate with excellent safety, and it is excellent in labor saving, safety and economy. We were able to supply the equipment.

以下、本発明を更に具体的に明らかにするために、本発明の実施形態について、図面を参照しつつ、詳細に説明する。   Hereinafter, in order to clarify the present invention more specifically, embodiments of the present invention will be described in detail with reference to the drawings.

先ず、図1には、本発明の一実施形態としての植物性粉粒体原料供給装置を含むガス発生装置の全体構造が概略的に示されている。又、図2には、植物性粉粒体供給装置の拡大概略図が、図3にはスクリューコンベアの概略図が示されている。   First, FIG. 1 schematically shows the entire structure of a gas generator including a plant powder raw material supply apparatus as one embodiment of the present invention. FIG. 2 shows an enlarged schematic diagram of the plant powder supply apparatus, and FIG. 3 shows a schematic diagram of the screw conveyor.

すなわち、図1中、炉体周壁10は厚肉の大径円筒形状を有しており、その内部に熱分解室が形成されている。そして、この熱分解室に、上部から供給された木粉等の粉粒体原料が堆積せしめられて、酸化・分解等の処理が施されるようになっている。なお、図面では省略してあるが、周壁は、例えば、耐火レンガ等で形成された内周壁と鉄筋コンクリート等で形成された外周壁の間に砂を充填した多層の耐火構造をもって形成される。また、周壁10の内周面は、略鉛直に延びる円筒形状の他、上方に向かって小径化するテーパが付された円筒形状であっても良い。更に、炉体のサイズは特に限定されるものでないが、実用的なサイズでは、周壁10の外径寸法や、高さ寸法は、何れも、数メートル以上にまで及ぶ。   That is, in FIG. 1, the furnace body peripheral wall 10 has a thick large-diameter cylindrical shape, and a pyrolysis chamber is formed therein. In this thermal decomposition chamber, powdery raw materials such as wood powder supplied from above are deposited and subjected to treatments such as oxidation and decomposition. Although omitted in the drawings, the peripheral wall is formed with a multilayer fireproof structure in which sand is filled between an inner peripheral wall formed of refractory bricks and an outer peripheral wall formed of reinforced concrete, for example. Further, the inner peripheral surface of the peripheral wall 10 may have a cylindrical shape with a taper that decreases in diameter toward the upper side in addition to a cylindrical shape that extends substantially vertically. Further, the size of the furnace body is not particularly limited, but in the practical size, the outer diameter and the height of the peripheral wall 10 both reach several meters or more.

また、炉体の下部にロストル(火格子)が設置されていると共に、このロストルの下方に配設された空気供給装置により、適当量のエアが熱分解室内に供給されるようになっている。なお、空気供給管は、適数本設置され得る。また、ロストル下部には、熱分解後の灰分や未分解木粉等を炉外に排出する掻き出し装置が配設されている。   In addition, a rooster (grate) is installed in the lower part of the furnace body, and an appropriate amount of air is supplied into the pyrolysis chamber by an air supply device disposed below the rooster. . An appropriate number of air supply pipes can be installed. Further, a scraping device that discharges ash after pyrolysis, undecomposed wood flour, and the like to the outside of the furnace is disposed at the lower part of the rooster.

また、炉体の上壁には、熱分解室において生成した発生ガスを、炉外に取り出すためのガス取出管が配設されており、該ガス取出し管に、ガス流量計やガス分析計が一般的に付置される。更に、炉内の温度を測定するための熱電対、圧力測定のための圧力センサー及び異常燃焼時の鎮火のための不活性ガス注入管を、炉内に付置してもよい。   In addition, a gas extraction pipe for taking out the generated gas generated in the pyrolysis chamber is disposed on the upper wall of the furnace body, and a gas flow meter and a gas analyzer are provided in the gas extraction pipe. Generally attached. Further, a thermocouple for measuring the temperature in the furnace, a pressure sensor for measuring pressure, and an inert gas injection pipe for extinguishing the fire in abnormal combustion may be installed in the furnace.

さて、炉体上部には、その中央部分を貫通して投入パイプ13が配設されている。この投入パイプ13は、円筒または角筒形状を有しており、その中心軸が鉛直方向に延びるようにして、炉体によって実質的に固定的に支持されている。ところで、かかる投入パイプ13は、下方に行くに従って次第に拡開するテーパを付してもよい。そして、投入パイプ13は、その上端部が炉体の上壁から所定高さで上方に突出せしめられている一方、その下端部が炉体の熱分解室に差し入れられている。   Now, in the upper part of the furnace body, a charging pipe 13 is disposed through the central portion thereof. The charging pipe 13 has a cylindrical or rectangular tube shape, and is substantially fixedly supported by the furnace body with its central axis extending in the vertical direction. By the way, the input pipe 13 may have a taper that gradually expands downward. The upper end portion of the charging pipe 13 is projected upward from the upper wall of the furnace body at a predetermined height, while the lower end portion thereof is inserted into the pyrolysis chamber of the furnace body.

そして、投入パイプ13の上部は、スクリューコンベア12の原料排出口と連結しており、その連結管22を通じて、木粉等の粉粒体原料が、押圧されながらスクリューコンベア12より投入パイプ13に供給される。木粉等の粉粒体原料は、この押圧作用により、投入パイプ内で棚つり現象などの不都合を生ぜずに、円滑に炉内に供給される。ここで、粉粒体の供給量は、スクリューコンベア12の回転速度により制御されうる。   The upper part of the input pipe 13 is connected to the raw material discharge port of the screw conveyor 12, and the powder material such as wood flour is supplied to the input pipe 13 from the screw conveyor 12 while being pressed through the connection pipe 22. Is done. The granular material such as wood powder is smoothly supplied into the furnace by this pressing action without causing inconvenience such as a shelving phenomenon in the input pipe. Here, the supply amount of the granular material can be controlled by the rotational speed of the screw conveyor 12.

次に、スクリューコンベア12上には、粉粒体原料タンク11が載置されて固設されている。この粉粒体原料タンク11は、図4の平面図に示されているように、円形の底壁と円筒形の筒壁を有する中空円筒状の容器であって、底壁の上面に沿って広がるように複数本の攪拌羽根を備えたプロペラ状の回転体が配設されており、燃料タンクの中心軸上に配設された回転支持軸によって支持されている。そして、この回転支持軸が電動モータで回動せしめられることにより、回転体が中心軸回りに回動作動するようになっている。そして、回転作動する攪拌羽根により、燃料タンク内の木粉等が外周側に向かって押圧して送られる作用が加えられるようになっている。   Next, on the screw conveyor 12, a powder material tank 11 is placed and fixed. As shown in the plan view of FIG. 4, the granular material raw material tank 11 is a hollow cylindrical container having a circular bottom wall and a cylindrical tube wall, and extends along the upper surface of the bottom wall. A propeller-like rotator provided with a plurality of stirring blades is disposed so as to spread, and is supported by a rotation support shaft disposed on the central axis of the fuel tank. The rotating support shaft is rotated by an electric motor, so that the rotating body rotates around the central axis. And the action | operation which the wood flour etc. in a fuel tank presses toward an outer peripheral side and is sent with the stirring blade which rotates is added.

さらに、粉粒体原料タンク11の底壁には、外周縁部と中心軸の中間部近くに位置して、原料排出口が貫設されており、この排出口と、スクリューコンベア12の原料受入口が連結管21により連結されている。これにより、粉粒体原料タンク11内の木粉等が、スクリューコンベア12内に導き入れられるようになっている。ここで、粉粒体原料タンクの原料排出口、連結管およびスクリューコンベアの原料受入口の形状は、長方形状、楕円状、円形状等の何れであってもよい。又、これに対応して、連結管形状は、長方形状、楕円状、円形状等をとりうる。   Furthermore, a raw material discharge port is provided in the bottom wall of the powder material raw material tank 11 near an intermediate portion between the outer peripheral edge portion and the central axis. The inlets are connected by a connecting pipe 21. Thereby, the wood powder etc. in the granular material raw material tank 11 are introduced into the screw conveyor 12. Here, the shape of the raw material discharge port of the granular material raw material tank, the connecting pipe, and the raw material reception port of the screw conveyor may be any of a rectangular shape, an elliptical shape, a circular shape, and the like. Correspondingly, the connecting pipe shape may be rectangular, elliptical, circular, or the like.

これにより、炉内での木粉等の消費減少分を安定的に供給するようになっていると共に、かかる投入パイプの内部が、常時、木粉等で充填されて、いわゆるマテリアルシール効果により、炉内で発生するガスの上方への流出が阻止されるようになっている。また、投入パイプ、スクリューコンベア及び粉粒体原料タンクの寸法並びに設備能力は、炉内の内法寸法や、木粉等の堆積高さ等を考慮して、木粉等の酸化や熱分解反応が安定して行われて、目的とする量の有効ガスを出来るだけ安定して採取することが出来るように、適当に設定されている。   As a result, the consumption reduction amount of wood powder and the like in the furnace is stably supplied, and the inside of the charging pipe is always filled with wood powder and the like due to the so-called material seal effect, The gas generated in the furnace is prevented from flowing upward. In addition, the dimensions and equipment capacity of the input pipe, screw conveyor, and powder material tank are determined based on the internal dimensions of the furnace, the height of the accumulated wood powder, etc. Is appropriately set so that the target amount of effective gas can be collected as stably as possible.

なお、粉粒体原料は、定法により粉粒体原料タンク11に導入される。例えば、図示しない外部の貯蔵タンクから、木粉等の粉粒体原料が、搬送ファンを用いたニューマチックコンベヤ等により、ホッパに供給され、更に、ホッパから、必要に応じて、粉粒体原料タンク11に導入される。   In addition, a granular material raw material is introduce | transduced into the granular material raw material tank 11 by a usual method. For example, a granular material such as wood powder is supplied from an external storage tank (not shown) to a hopper by a pneumatic conveyor using a conveyance fan, and further, from the hopper, if necessary, a granular material. It is introduced into the tank 11.

平均粒径1mmの木粉を、その低壁に幅40cm、長さ1.5mの長方形型原料排出口を有する直径2m、高さ1.4mの粉粒体原料タンクに供給し、該タンク底壁の上面に沿って広がるように4本の攪拌羽根を備えた回転プロペラにより、毎時3mの木粉を、該排出口から連結管を通してスクリューコンベアに排出した。この時の回転プロペラには、動力2.2kwで1/20減速機つきのモータを使用した。 The wood powder with an average particle diameter of 1 mm is supplied to a powder raw material tank having a diameter of 2 m and a height of 1.4 m having a rectangular raw material discharge port having a width of 40 cm and a length of 1.5 m on its lower wall. With a rotating propeller equipped with four stirring blades so as to spread along the upper surface of the wall, 3 m 3 of wood flour per hour was discharged from the discharge port to the screw conveyor through the connecting pipe. As the rotating propeller at this time, a motor with a power of 2.2 kw and a 1/20 speed reducer was used.

上記粉粒体原料タンクから送られてきた木粉を、断面形状が幅40cm、長さ1.5mの角筒形状を有する連結管を通して、同等の原料受入口寸法を有するスクリューコンベアに供給し、該スクリューコンベアの原料排出口(幅40cm、長さ40cmの正方形状)から、同等の断面形状を有する連結管を通して投入パイプ内に圧送した。該スクリューコンベアには、外径38cm、長さ2m、スクリュー羽根のピッチ25cm、動力2.2kw、400rpmのものを使用した。又、該スクリューコンベアは、バイオマスガス炉の上部に、原料受入口を上として、15度の傾斜で載置された。 The wood powder sent from the above-mentioned granular material raw material tank is supplied to a screw conveyor having an equivalent raw material inlet dimension through a connecting pipe having a square tube shape with a cross-sectional shape of width 40 cm and length 1.5 m, From the raw material discharge port (a square shape having a width of 40 cm and a length of 40 cm) of the screw conveyor, it was pressure-fed into the charging pipe through a connecting pipe having an equivalent cross-sectional shape. The screw conveyor having an outer diameter of 38 cm, a length of 2 m, a screw blade pitch of 25 cm, a power of 2.2 kw, and 400 rpm was used. In addition, the screw conveyor was placed on the upper part of the biomass gas furnace with a 15-degree inclination with the raw material receiving port at the top.

次に、上記スクリューコンベアから圧送されてきた木粉を、幅40cm、長さ40cm高さ10cmの角筒を通じて、投入パイプに供給した。この時用いた投入パイプは、上部開口部(幅40cm、長さ40cm)、下部開口部(幅50cm、長さ50cm)、高さ1mで、下方に拡開したテーパ状のものを使用した。なお、上記の粉粒体原料タンク、スクリューコンベア、投入パイプ及び各連結管の何れも鋼製のものを用いた。   Next, the wood powder fed from the screw conveyor was supplied to the charging pipe through a square tube having a width of 40 cm, a length of 40 cm, and a height of 10 cm. The input pipe used at this time was an upper opening (width 40 cm, length 40 cm), a lower opening (width 50 cm, length 50 cm), a height of 1 m, and a taper-shaped pipe that expanded downward. Note that all of the above powder material tank, screw conveyor, charging pipe and connecting pipes were made of steel.

上記構成の原料供給装置により、投入パイプ内で粉粒体原料の詰まりを生ずることなく、円滑に原料供給が可能であった。   With the raw material supply device having the above-described configuration, the raw material could be supplied smoothly without causing clogging of the granular material in the charging pipe.

粉粒体原料供給装置を含むバイオマス変換式ガス発生炉の装置構成を示す概略図である。It is the schematic which shows the apparatus structure of the biomass conversion type gas generating furnace containing a granular material raw material supply apparatus. 粉粒体原料供給装置の構成を示す概略図である。It is the schematic which shows the structure of a granular material raw material supply apparatus. スクリューコンベアを示す概略図である。It is the schematic which shows a screw conveyor. 粉粒体原料タンクを示す平面概略図である。It is a plane schematic diagram showing a granular material raw material tank.

符号の説明Explanation of symbols

10 炉体周壁
11 粉粒体原料タンク
12 スクリューコンベア
13 投入パイプ
21 粉粒体原料タンクとスクリューコンベアの連結管
22 スクリューコンベアと投入パイプの連結管
DESCRIPTION OF SYMBOLS 10 Furnace peripheral wall 11 Granule raw material tank 12 Screw conveyor 13 Input pipe 21 Connection pipe of powder raw material tank and screw conveyor 22 Connection pipe of screw conveyor and input pipe

Claims (1)

筒型の周壁部を備えた竪型中空の炉体上方に設置した粉粒体原料タンクから、木粉等の植物性粉粒体原料を、該炉体の上部を貫通して配設した投入パイプを通じて、該炉体の内部に供給しつつ、該炉体の内部で植物性粉粒体原料を熱分解せしめて発生ガスを炉外に吸引収集するようにしたバイオマス変換式ガス発生装置において、粉粒体原料タンクと投入パイプの中間部にスクリューコンベア(Screw conveyor)を配設し、該粉粒体原料タンクの原料排出口とスクリューコンベア(Screw conveyor)の原料受入口、及び、該スクリューコンベア(Screw conveyor)の原料排出口と投入パイプの上部開口部が、各々連結管により連結されたバイオマス変換式ガス発生炉用植物性粉粒体原料供給装置。
From the powder material tank installed above the vertical hollow furnace body with a cylindrical peripheral wall, plant powder material such as wood flour is placed through the top of the furnace body. In the biomass conversion type gas generator that is supplied to the inside of the furnace body through the pipe, and the plant powder raw material is pyrolyzed inside the furnace body and the generated gas is sucked and collected outside the furnace, A screw conveyor (Screw conveyor) is arranged in the middle of the powder material tank and the input pipe, a material outlet of the powder material tank, a material inlet of the screw conveyor, and the screw conveyor (Screw conveyor) A raw material supply device for a biomass conversion gas generator for a biomass conversion gas generator, in which the raw material outlet and the upper opening of the input pipe are each connected by a connecting pipe.
JP2003418816A 2003-12-17 2003-12-17 Apparatus for feeding granular raw material for biomass conversion type gas producer Pending JP2005179405A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2003418816A JP2005179405A (en) 2003-12-17 2003-12-17 Apparatus for feeding granular raw material for biomass conversion type gas producer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2003418816A JP2005179405A (en) 2003-12-17 2003-12-17 Apparatus for feeding granular raw material for biomass conversion type gas producer

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JP2005179405A true JP2005179405A (en) 2005-07-07

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