JP5650812B1 - A system that converts organic matter such as biomass into a heat source for multiple combustion and converts it to steam for power generation - Google Patents
A system that converts organic matter such as biomass into a heat source for multiple combustion and converts it to steam for power generation Download PDFInfo
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- 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
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/12—Heat utilisation in combustion or incineration of waste
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- 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
- Y02E50/10—Biofuels, e.g. bio-diesel
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- 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
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- 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
- Y02P20/10—Process efficiency
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Abstract
【課題】人の生活にとって不可欠の電気を膨大な未利用資源を重複活用する手段を積み重ねて発電に至るシステムを構築する。【解決手段】先願技術を継承改良して上記課題に至る手段を複次積み重ねるもので、先ず未利用資源である有機体を熱源とするには物質特性上先ず純炭素状まで進めなければならないので改良を積み重ねた炭化手段装置を構築し、その出来た純炭素材（グラファイト）を原子状態まで改質しながら高温空気の原子状酸素と反応させて輻射熱源化し、その輻射熱線光波を高率の熱交換機能のあるボイラーで一次湿り蒸気にし、更にその蒸気圧を活用する転換装置で高温廃ガスを誘引して二次過熱蒸気化し、その改良蒸気タービンで受けてトルクの大きい回転力に換え、その特性に合わせて多極型発電機を駆動して電気を得るシステムである。【選択図】図３To build a system that accumulates means for utilizing a large amount of unused resources for electricity essential for human life and leads to power generation. [Means for solving the problems] The means to reach the above-mentioned problems by inheriting and improving the technology of the prior application is piled up. First, in order to use an organic material which is an unused resource as a heat source, it must first proceed to a pure carbon state in terms of material characteristics. Therefore, we built a carbonization means device that has been repeatedly improved, reacting it with atomic oxygen in high-temperature air while reforming the resulting pure carbon material (graphite) to the atomic state, and generating a high rate of radiation heat ray The boiler with heat exchange function is used to make primary wet steam, and a high-temperature waste gas is drawn into secondary superheated steam by a conversion device that uses the steam pressure, and it is received by the improved steam turbine and converted to a torque with a large torque. This is a system that obtains electricity by driving a multipolar generator in accordance with its characteristics. [Selection] Figure 3
Description
本発明は先願技術を継承改良し移動可能な連継システム装置の開発を目指しバイオマス等有機体を乾溜炭化をして高品質燃料化し、重複燃焼発熱させ効率よく熱交換して高圧蒸気に変換し、蒸気タービンで回転動力に換え、その動力によって発電するシステム技術装置に関するものである。 The present invention inherits and improves the technology of the previous application and aims to develop a transfer system that can be moved. Carbonized organic matter such as biomass is carbonized into high quality fuel, and heat is generated by overlapping combustion to efficiently exchange heat and convert to high pressure steam. In addition, the present invention relates to a system technology device that generates electric power by using a rotatory power instead of a steam turbine.
生産と生活の結果として巷に満ちあふれる産業廃棄物的未利用資源は危機的な状況にある。その可燃物を焼却処分するにしても人の健康を阻害するに至る環境汚染をもたらすおそれもあり、その処理に膨大なコストの負担を強いられている。
しかし自燃力のある資源を高品質な燃料化し、有効に燃焼発熱熱源として効率よく熱交換し高圧蒸気に変換して発電出来れば、その資源価値は莫大なものとなる。そのシステム技術に立遅れがあり、普遍的な技術の開発が焦眉の社会的急務となっている。
As a result of production and livelihood, the wasteful industrial waste resources are in a critical situation. Even if the combustible material is incinerated, there is a risk of environmental pollution leading to human health, and the treatment is forced to bear an enormous cost.
However, if resources with self-combustion power are converted to high-quality fuels, they can be efficiently exchanged heat as a combustion heat source and converted into high-pressure steam to generate electricity, the resource value will be enormous. The system technology is lagging behind, and the development of universal technology has become a keen social urgent task.
前項に鑑み本発明者は資源の有効な活用に参画し、それ等の資源を有効な熱に変換する具体的方策と技術を提言して来たので逐次記述する。
燃焼熱を利用する為に物質を燃やす行為は古来から連綿として行われている。限られた装置内で効率よく熱に転換するには燃焼雰囲気を高温に維持して発熱体を高温化し、その燃焼炎輻射熱線の電磁波化して可能な限り電熱面積を広く確保することである。発明者等が出会った現象をもとに仕上げた火炎を包み込む高圧少量の斜め対向流送風手段によって具現された事象は、ステファン・ボルツマンの法則による事象でもあった。発明者は更に炉壁を遠赤外線放射機能の高い炉材を選んで構築し、負圧状況の中で最小限の空気量に限定する斜め高圧対向流送風との相乗作用によって燃焼炎を高温遠赤外線輻射熱線化する域に到達した。燃焼雰囲気の高温維持は炭素分子と酸素分子の各原子化工程の解離エネルギーを供給する効果ともなり総合エネルギー収支理論に合致した乾溜ガス化燃焼事象でもある本願の燃焼熱交換部分の基礎とも成った。
In view of the preceding paragraphs, the present inventor has participated in the effective use of resources and has proposed specific measures and techniques for converting those resources into effective heat, and will be described sequentially.
The act of burning a substance to use the heat of combustion has been practiced continuously since ancient times. In order to efficiently convert to heat in a limited apparatus, it is necessary to maintain the combustion atmosphere at a high temperature to increase the temperature of the heating element and to convert the combustion flame radiation heat rays into electromagnetic waves so as to ensure as wide an electric heating area as possible. The event embodied by the high-pressure and small-scale oblique counter-flow fan that wraps the flame finished based on the phenomenon that the inventors met was also an event according to Stefan-Boltzmann's law. The inventor further constructed the furnace wall by selecting a furnace material with a high far-infrared radiation function, and the combustion flame is heated to a high temperature by synergistic action with the oblique high-pressure counter-flow fan that limits the amount of air to the minimum in the negative pressure situation. Reached the area where infrared radiant heat rays are generated. Maintaining the combustion atmosphere at a high temperature has the effect of supplying dissociation energy for each atomization process of carbon and oxygen molecules, and has also become the basis for the combustion heat exchange part of the present application, which is a dry distillation gasification combustion event that meets the overall energy balance theory. .
物質が燃えるという化学反応は原子炭素と原子酸素がその条件を得て燃焼反応して熱を発生することであるが、その各分子状から各原子状になる為には膨大な解離エネルギーを必要とする。例えば分子状炭素と酸素が燃焼の場合３／４がそれに使われるので実際外部に利用されるのは１／４に過ぎない。結合エネルギー収支理論によると有機体が炭素状態に分解するには亦更に多くの解離エネルギーを奪われるので燃焼熱として外部にでる反応熱は目減りすることになり、有機体の熱量が小さいといわれるゆえんである。
発明者は未利用資源を効率の高い燃料とする為に、それが限りなく炭素分子状に近い炭化材とする目的で遠赤外線光波の力を借りる無酸素雰囲気の中で物体を燃やすことなく乾溜ガス化する化学反応にたよって炭化する方法を追い続けて来た。ようやく純度の高い炭素材とコスト面でも社会に適用する段階に到達したので、その成果による炭化材或いは乾溜材化工程を経過した物材を燃料として効率的熱源に生かす本願に到達した。The chemical reaction that a substance burns is that atomic carbon and atomic oxygen get the conditions and generate a heat reaction to generate heat, but enormous dissociation energy is required to change from each molecular state to each atomic state. And For example, when molecular carbon and oxygen are used for combustion, 3/4 is used for it, so only 1/4 is actually used outside. According to the bond energy balance theory, when an organism decomposes into a carbon state, more dissociation energy is lost, so the reaction heat that appears outside as combustion heat is reduced, and it is said that the amount of heat of the organism is small. It is.
The inventor made dry distillation without burning an object in an oxygen-free atmosphere that borrows the power of far-infrared light waves in order to make the unused resources a highly efficient fuel, in order to make it a carbonaceous material that is nearly carbon molecular. We have continued to follow the method of carbonization according to the chemical reaction to gasify. Finally, we have reached the stage of applying it to society in terms of high purity carbon material and cost, so we have arrived at the present application that uses the carbonized material resulting from the result or the material that has undergone the dry distillation process as an efficient heat source as fuel.
燃焼と熱交換の効率を大幅にアップした蒸気によるベンチュリスクラバ機構によって、高熱の燃焼排ガスを誘引して高温融合変換蒸気化し、その圧力を回転力転換する接点となる蒸気タービンには合成正弦曲線を基調とした羽根形の蒸気タービンを開発した。それによって小規模装置で中圧大容量の蒸気も効率よくトルクの大きい回転力に変換できる。 The steam venturi scrubber mechanism with steam that greatly improves the efficiency of combustion and heat exchange induces high-temperature combustion exhaust gas into high-temperature fusion conversion steam, and a synthetic sine curve is formed on the steam turbine that becomes the contact point that converts the rotational force of the steam A basic vane-shaped steam turbine was developed. As a result, it is possible to efficiently convert steam with medium pressure and large capacity into a rotational force with a large torque with a small-scale device.
炉壁を構築する新規材料の起源は非特許文献３，４，５，６の通りである。 The origin of the new material for constructing the furnace wall is as described in Non-Patent Documents 3, 4, 5, and 6.
前項の積み重ねを受けて、本発明者はその具体的利用目標について鋭意考察した結果、普遍的需要のある電気に変換再生することに目標を定めた。その未達の技術開発が進めば、廃棄物的未利用資源は厄介物転じて宝の山となる。本願は緊急を要する社会的要請の解決と確実な社会需要とを結ぶシステム技術の開発を目指す。具体的装置としては膨大な資源材料の存在する現場に移動可能な装置を造成することを目指す。 Following the accumulation of the previous paragraph, the present inventor intensively studied the specific utilization target, and as a result, set a goal to convert and regenerate electricity with universal demand. If the undeveloped technological development advances, waste-based unused resources turn into troublesome things and become treasures. This application aims to develop a system technology that links urgent social demands with certain social demands. As a specific device, we aim to create a device that can be moved to the site where a huge amount of resource materials exist.
本システムを進めるいくつかの装置は機能面で遠赤外線放射機能炉壁を備えることが必須とされているので、まずその原材料の準備から始め、炉壁構築に進みたい。 Since some devices that advance this system are required to have a far-infrared radiation functional furnace wall in terms of functionality, we want to start with the preparation of the raw materials and then proceed to the furnace wall construction.
本願装置の特徴である熱交換燃焼炉や炭化炉等の炉床と炉壁を構成する材料について考察説明する。
（１）ライフグリーンは石川県金沢市医王山に産出する石英祖面並に結晶メノー含有パーライト系岩で構成され平均した組成分はＳｉＯ２‐７５．５３％、Ａｌ２Ｏ３‐１３．３４％、Ｆｅ２Ｏ３−０．７６％、ＣａＯ−１．３３％、Ｎａ２Ｏ‐３．６５％、Ｋ２Ｏ−３．４３％、ＭｇＯ‐０・１６％、ＴｉＯ２−０．１２％等を含有する外、エマナチオン（ＲＨ）を含み、土中では酸素富化現象を呈、とにかく硬い特性をもつ。
（２）アルミナセメントは遠赤外線放射力も強く、各材料を混練するに当たってバインダーとして優れた性能を持っている。
（３）牡蠣殻焼成石灰‐牡蠣殻は５７％のＣＯ２を含有する炭酸石灰状で、それを１，２００℃のキルーンで焼いても２０％弱しか生石灰化せず４０％近いＣＯ２は炭酸石灰状のままである（岩手工技センター）
（４）高濃度ホウ酸複合化合液は、（イ）高分子特性のあるパーム椰子殻焼成灰（５ｋｇ）を（ロ）特殊腐植物質を加工したマリネック抽出液（２０リットル）で抽出された残液（１０リットル）を温め（４０℃）（ハ）ホウ酸１０ｋｇと硫酸マンガン（１ｋｇ）、２０ｋ圧を示して全く溶けない特性でもある。The material constituting the hearth and wall of the heat exchange combustion furnace, carbonization furnace or the like, which is a feature of the present apparatus, will be described.
(1) Life Green composition fraction averaged composed of crystal agate containing pearlitic rock quartz its surface parallel to yield the Iozen Kanazawa Ishikawa SiO 2 -75.53%, Al 2 O 3 -13. 34%, Fe 2 O 3 -0.76 %, CaO-1.33%, Na 2 O-3.65%, K 2 O-3.43%, MgO-0 · 16%, TiO 2 -0. In addition to containing 12%, etc., it contains emanathione (RH), exhibits an oxygen enrichment phenomenon in the soil, and has a hard property anyway.
(2) Alumina cement has strong far-infrared radiation, and has excellent performance as a binder in kneading each material.
(3) Oyster shell calcined lime-Oyster shell is in the form of carbonated lime containing 57% CO 2 , and even if it is baked in a kiln at 1,200 ° C., only 20% is quick-calcified and CO 2 is nearly 40%. It remains in the form of lime carbonate (Iwate Engineering Center)
(4) The high-concentration boric acid composite compound mixture is obtained by extracting (i) palm coconut shell calcined ash (5 kg) having high polymer characteristics with (b) marineck extract (20 liters) processed from special humic substances. The liquid (10 liters) is warmed (40 ° C.). (C) 10 kg boric acid and manganese sulfate (1 kg).
前項３種を混和したものを高濃度ホウ酸複合化合液で混練すると漆黒の混合材の炉壁材となるので、分解した外壁鉄板に内装し、熱線放射型電気炉で窒素ガス置換焼成して組立てる。
初回熱処理時１，２００℃では溶解し、１，０００℃で安定した黒色材となり、窒素ガス置換では７００℃では陶器状となったので実施時の温度帯については慎重に検討を要する。
上記基材３種それぞれ遠赤外線放射機能につながる特性成分を持ち、更にマイナスイオンの磁性を帯びるといわれるものが数種あり、その合成放射機能への期待が高い。
また特許文献４、の取組み事象の例として複数材料を高濃度ホウ酸複合化液で練り合わせた際に前記牡蠣殻をキルーンで１，２００℃で焼成した白色の牡蠣殻燃成粉砕物を加えた時、その混合物が漆黒に変化した。乾燥後、電気炉で１，０００℃で焼成後の一関高専の分析結果では炭素の集積が非常に高い結果を得た。表図−１に示す様に炭素が重量で３０％で、分子数で５６％の数値からは他の基材からはその炭素が見出せず、４５％余の炭酸ガスを抱え込んでいるという牡蠣殻焼成粉砕物内の炭酸ガスが酸素を放出し炭素が残溜したとすればほぼ理解できる数値であり、牡蠣殻中の炭酸ガスが還元的分解反応し易いこと教えるものと考えれば、その後望外の牡蠣殻活用の希望を与えられた。本願での炉壁機能としての域では通電性は見られないとのことであったので、炉壁からの光波の発進に好影響への期待が高い。
At the first heat treatment, it melts at 1,200 ° C. and becomes a stable black material at 1,000 ° C., and when it is replaced with nitrogen gas, it becomes a pottery shape at 700 ° C. Therefore, careful examination of the temperature zone at the time of implementation is required.
Have the characteristics components leading to the substrate 3 or the respective far-infrared radiation function, there still several what is said magnetized negative ions, high expectations for its synthesis radiation function.
Further, as an example of the action event of Patent Document 4, white oyster shell combustible pulverized material obtained by firing the oyster shell at 1,200 ° C. in a kiln when a plurality of materials were kneaded with a high-concentration boric acid complex solution was added. At that time, the mixture turned jet black. The analysis result of Ichinoseki National College of Technology after drying and firing in an electric furnace at 1,000 ° C. showed that carbon accumulation was very high. As shown in Table 1, carbon is 30% by weight and the number of molecules is 56%. From the other base materials, the carbon cannot be found from other base materials, and the oyster shell contains 45% or more carbon dioxide gas. If carbon dioxide in the baked pulverized product releases oxygen and carbon remains, it is a numerical value that can be almost understood, and if you think that carbon dioxide in oyster shell is easy to undergo reductive decomposition reaction, I was given the hope of using oyster shells. In the area of the furnace wall function in the present application, no electrical conductivity is seen, so there is high expectation for a positive effect on the start of light waves from the furnace wall.
本発明者は多様な物質循環策を開発しているが、膨大な未利用資源、特にも主題のバイオマスを燃料として有効な熱に変換するに当って、後述する燃焼等の利用技術以前に、資源を燃料化する前提について考慮すべきことについて学術文献に教導された。燃焼とは物質の燃えることであるが、それは物資がガス化、つまり炭素、酸素それぞれが原子化して結合反応する化学反応であり、その次元から越えねばならない原理がある。その反応の実態を検証すると、炭素原子と酸素原子が衝突反応して二酸化炭素となるに当って発熱する現象の熱収支法則がある。その基本に関わる木質系炭の純粋な炭素体の燃焼を例にして、現象の基礎である化学反応における総合エネルギー理論の観点から燃焼反応にかかるエネルギー収支の推移を知ることが、その後の技術対応の方向性を探る基礎となる。それを表−２に示す。
上記高温原子状炭素ガスと高温原子状酸素との結合反応の設定単位当りの総合熱量収支３８３ｃａｌのうち分子状炭素と分子状酸素との燃焼反応の場合では我々が利用出来るのは、ＣＯ2ガス化反応熱のうち吸熱分の差引余剰となる９５ｋｃａｌだけで、約４分の１という現実である。（グラファイトは炭素原子２ケの結合分子体）
上記反応熱を利用を目的とする立場からの検証結果に教えられて、バイオマス等有機体を物質循環する一端として燃料化を考えれば、限りなく炭素分子状に近づいた状態にすることが、限られた熱交換燃焼装置における効率向上の為に求められる。反対に、炭素分子体から遠ざかる有機体個体は解離吸熱反応を幾段階も重ねることになり、反比例してロスが多くなることを知ると共に、燃焼循環の重要さも思い知らされた。各因子分子に解離エネルギーを与える有機体素材を純炭素材（グラファイト）燃料にすることが資源再生のスタートになるという本願思考の起源である。
Of the total calorie balance 383cal per set unit of the bonding reaction between the high temperature atomic carbon gas and high temperature atomic oxygen, in the case of the combustion reaction between molecular carbon and molecular oxygen, we can use CO2 gasification Only 95 kcal, which is a surplus of the endothermic portion of the reaction heat, is a reality of about a quarter. (Graphite is a binding molecule with two carbon atoms)
Given the verification results from the standpoint of utilizing the heat of reaction described above and considering fuel conversion as one end of material circulation of organic substances such as biomass, it is possible to limit the state to a carbon molecular shape as much as possible. It is required for improving the efficiency of the heat exchange combustion apparatus. On the other hand, it was found that an individual organism moving away from a carbon molecule would undergo a number of dissociative endothermic reactions, and the loss increased in inverse proportion, and the importance of combustion circulation was also realized. The origin of the present application is that the organic material that gives dissociation energy to each factor molecule is made of pure carbon (graphite) fuel, which starts the resource regeneration.
本発明者は木質系をはじめとするバイオマス等を燃料として発電需要につなげる前提として、グラファイトに限りなく近づける炭化手段を特許第４２２００８３号にたどりついたが、出願（平成１１年）後その原理を検証すべく次の手段を実施した。外熱による鉄箱の内側の遠赤外線放射機能のもとで、窒素ガス雰囲気（無酸素）のなかで乾溜変化によって得られた試験経緯結果を表−3に示す。
上記処理によって得られた炭化材（雑木乾燥材最大５×１０×１５ｃｍ角）は非常に軽いものであったが、岩手県工試の分析によると、グラファイト８，１００ｃａｌ／ｇとの対比で９４％〜９８％の発熱量をもつ炭化材（７，５００ｃａｌ／ｇ）であることが確かめられ、奇跡的結果が得られ、その後の発想に重要な示唆となり、本システムのスタートとなる有機体を高能率燃料体に進化させるという方向性が定まった。また前記試験における鉄箱から吹出す気化ガスが、周囲からの加熱によって３５０℃段階で着発火したことも、その後の開発に重大な示唆を与えられた。
The present inventor has arrived at Patent No. 4220083 as a premise to connect woody and other biomass to power generation demand using fuel as a fuel, but after the application (1999), the principle was verified. The following measures were implemented. Table 3 shows the test results obtained by dry distillation change in a nitrogen gas atmosphere (oxygen-free) under the far-infrared radiation function inside the iron box by external heat.
The carbonized material obtained by the above treatment (mixed wood drying material maximum 5 × 10 × 15 cm square) was very light, but according to the analysis by Iwate Prefecture Engineering Test, it was 94 in comparison with graphite 8,100 cal / g. % -98% calorific value (7,500 cal / g) was confirmed, and miraculous results were obtained. The direction to evolve into a highly efficient fuel body has been determined. In addition, the vaporization gas blown out from the iron box in the above test ignited in the 350 ° C. stage by heating from the surrounding area also gave a serious suggestion to the subsequent development.
以下、主題について順を追って具体策を説明する。
（Ａ）−発明者は物質の燃焼熱を活かす立場から、燃焼を考える技術として高能率熱交換燃焼装置−特許第３０３０３２１号を発案しそれに基いた改善策を提案している。即ち、燃料比較対比で容積の大きい遠赤外線放射力の強い炉壁を備えた熱交換燃焼室（４５ｃｍ×４５ｃｍ×１８０ｃｍ炉）の中で、強い負圧に引かれ吸引空気で燃える燃焼物から発生する４リットルバーナー炎を包み込む様に炎の流れに対向し斜めに横断して単列或いはラッパ状の高温化された高圧空気膜を噴射して強烈な燃焼反応層を形成させて輻射熱バリア化し、それに包み込まれて燃焼炎が高温となって乾溜ガス化が進み、炎は輻射熱線化して周囲の間隙を有して並列された熱交換水管壁に輻射熱を直照射され、同時に熱せられた炉壁からは遠赤外線が反射されて水管の熱交換が進行し−対向流送風ガス化溶融燃焼と呼べるステファン・ボルツマン法則事象を典型的に活かせる技術である。
ステファン・ボルツマンの法則とは又放射線光波機能でもある。｛燃焼温度＋２７３℃｝４＝輻射熱線→電磁波（熱交換効率が高い）（特許文献１）
In the following, specific measures will be explained in order for the subject.
(A)-From the standpoint of utilizing the combustion heat of a substance, the inventor proposed a highly efficient heat exchange combustion apparatus-Patent No. 3030321 as a technique for considering combustion and has proposed an improvement measure based on it. In other words, in heat exchange combustion chamber (45cm × 45cm × 180cm furnace) equipped with a furnace wall with a large volume of far-infrared radiation compared with fuel comparison, it is generated from combustion products that are attracted by strong negative pressure and burned with suction air In order to wrap the 4 liter burner flame, it is opposed to the flame flow, obliquely traversing it and injecting a single-line or trumpet-like high-temperature high-pressure air film to form a strong combustion reaction layer to form a radiant heat barrier, Enclosed in it, the combustion flame becomes high temperature and dry distillation gasification progresses, the flame is converted to radiant heat radiation, and the heat exchange water pipe walls arranged in parallel with the surrounding gap are directly irradiated with radiant heat, and the furnace is heated at the same time The far-infrared rays are reflected from the walls and heat exchange of the water tubes proceeds-a technique that can typically take advantage of the Stefan-Boltzmann law phenomenon, which can be called counterflow blast gasification melt combustion.
Stefan Boltzmann's law is also a radiation lightwave function. {Combustion temperature + 273 ° C} 4 = Radiant heat rays → Electromagnetic waves (high heat exchange efficiency) (Patent Document 1)
本項のステファン・ボルツマンの法則事象の現象を別の視点からみると、前記燃焼手段によって燃焼雰囲気を高めることは炭素分子、酸素分子に解離エネルギーを与えることになると共にその熱線の直進性を活かす熱交換手段効果になり、比例して燃焼反応熱が増えることになる。
バイオマス等を燃やして熱を求めるに際しては、その物質特性から越えなければならない課題が多いことを教えられた。段落番号００１２項で示している表−２によると、燃焼反応が起きるには、炭素と酸素がそれぞれ原子化しなければならない化学的定めがあり、それから遠く離れた有機体は解離吸熱反応を幾段階も越えなければならなので、効率的に燃焼反応熱を求めるには、まず素材を完全な炭素体に近づけなければならないという宿命にあることから、それに可能な限り近づきたい。段落番号００１２項に示した表−2から教えられた現象から本システム構成の目標が定まり、以下順序に示したい。
Looking at the phenomenon of Stefan-Boltzmann's law phenomenon in this section from another viewpoint, increasing the combustion atmosphere by the combustion means gives dissociation energy to carbon molecules and oxygen molecules and makes use of the straightness of the heat rays. It becomes a heat exchange means effect, and the heat of combustion reaction increases in proportion.
I was told that there are many issues that must be overcome from the material characteristics when burning biomass and so forth to obtain heat. According to Table-2 shown in paragraph No. 0012, there is a chemical definition that carbon and oxygen must be atomized in order for the combustion reaction to take place, and an organism far away from it has several steps of dissociative endothermic reaction. Therefore, in order to obtain the heat of combustion reaction efficiently, the material must be brought close to a complete carbon body, so we want to approach it as much as possible. The target of this system configuration is determined from the phenomenon taught from Table-2 shown in paragraph 0012, and I would like to show it in the following order.
（Ｂ）‐バイオマス等有機体をグラスファイト態に進化させる一方法は次の通りである。
（イ）ハンマークラッシャーで細断した素材チップが自然流下する傾斜炉は（図‐１）横断面は底面を９０ｃｍとする長楕円半円形高さ１ｍで長さ１．８ｍの鉄板製で、炉内壁に遠赤外線機能壁を内装した傾斜炉２〜３基を組合わせそれを設置する架台は５５°程度の傾斜として、素材が自然流下の状態に合わせて再調製し、炉底裏下に耐火レンガを側壁とする燃焼室を設けてバーナー熱源と対向流送風装置を組合わせた完全燃焼排ガス発生桟構としてその無酸素状排ガスを傾斜炉上部の通路より内部に吸引して流下材料を加熱する桟構を設け、頂部円形部分を下方から吸引負圧に引かれて発熱体の燃焼２次排熱ガスが流動する、上端に素材供給口を設け炉外に原料供給口を設け、下端面の上部に気化ガス排出口を、下端下部に炭化材の排出装置を設け、外部に水冷却スクリューを接続し、水又は蒸気による消火冷却機構を付設する。気化ガスは下端上部の排出口からの吸引力に引かれて降下し、排出口に連接するボイラーへの移送管を通ってボイラーに送られ燃焼される機構である。
前述の機構に基づき上端の素材供給口から素材チップが供給され、炉底面を流下するチップは炉上面を流下する発熱体の燃焼２次排ガス熱源と、炉壁からの遠赤外線光波との相乗作用を受けて過熱蒸気雰囲気のもと酸欠乾溜機構の作用が働き完全炭化材（グラスファイバー）への変化が進み、気化機能作用で発生した気化ガスはボイラーから負圧吸引力に引かれて下降しボイラーに吸い込まれる。
下端の炭化材排出口での状況を調べながら上部チップ供給装置からの供給量を調節する仕様となる。(B)-One method for evolving an organism such as biomass into a glass fight state is as follows.
(B) Inclined furnace in which the material chips shredded by hammer crusher naturally flow down (Fig. 1) The cross section is made of an iron plate with an elliptical semicircular height of 1 m and a length of 1.8 m with a bottom of 90 cm. Combined with two or three tilt furnaces with far-infrared functional walls on the inner wall, the installation base is inclined at about 55 °, the material is re-adjusted according to the state of natural flow, and refractory under the furnace bottom As a complete combustion exhaust gas generating frame combining a burner heat source and a counterflow air blower with a brick-side combustion chamber, the oxygen-free exhaust gas is sucked into the passage from the upper part of the inclined furnace to heat the flowing material. A frame is provided, the top circular part is drawn from below by suction negative pressure, and the combustion secondary exhaust heat gas of the heating element flows, a material supply port is provided at the upper end, a raw material supply port is provided outside the furnace, Vaporized gas discharge port at the top and carbonized material discharge at the bottom bottom The location provided to connect the water cooling screw to the outside, to attaching a fire extinguishing cooling mechanism with water or steam. The vaporized gas is drawn down by the suction force from the discharge port at the upper end of the lower end, and is sent to the boiler through the transfer pipe to the boiler connected to the discharge port and burned.
Based on the above-mentioned mechanism, the material chip is supplied from the material supply port at the upper end, and the chip flowing down the furnace bottom surface is a synergistic action between the heat source of combustion secondary exhaust gas flowing down the furnace top surface and the far-infrared light wave from the furnace wall In response to the superheated steam atmosphere, the oxygen-depleted dry distillation mechanism works and the transition to completely carbonized material (glass fiber) progresses, and the vaporized gas generated by the vaporization function is pulled down by the negative pressure suction force from the boiler. It is sucked into the boiler.
It becomes a specification to adjust the supply amount from the upper chip supply device while examining the situation at the carbide outlet at the lower end.
(ロ)斜傾炉で発生した気化ガスは、炉と一体連接機構のボイラーに吸い込まれ燃焼される。そのボイラー構造は（図２）の様に立型円形で基部炉は炉壁１５ｃｍ厚の炉壁内径1mの高さ５０ｃｍの鉄板製で、気化ガス吸入口と対象位置に着火バーナー口を、周り中間位置に温度検知口を備え、熱交換部は、基部炉の上に内径１ｍで高さ8ｃｍ、巾８ｃｍの下端角型円周径管の上に高さ２ｍの５ｃｍ径管を２．５ｃｍの間隔をあけて円周配列し、上端に横巾８ｃｍ、高さ２５ｃｍで、上面を半円形の角型円周型管でつないで気水分離室として蒸気圧力弁を備え、熱交換本体の貫流水管の外側は遠赤外線放射機能炉壁材を内装（５ｃｍ厚）した鉄板外壁で囲み、内径２０ｃｍ径の煙突基部装置を備えた円形炉壁板で閉じる。煙突基部装置には煙突分流口を備え、対象位置に有意のパイプ穴と中間周位置に温度検知口を設け、上部には十分な吸引力のある煙突を立て、パイプ穴には有意径パイプに炉外位置にチャッキバルブで中継ぎの高圧送風機を備え、煙突中心位置で直角下降し、貫流水管長半分の位置に、下方鋭角のラッパ型高圧送風膜口装置を設け、熱交換水は貫流水管下端円周管にカスケードポンプで供給される。
吸引負圧力の強い煙突機能によって、炭化装置からの気化ガスがボイラー内に吸い込まれるとバーナーが噴射されガスは火災化し、炎が安定したなら着火バーナーは消され炉中段の高圧送風機構が作動して輻射バリヤが形成され、包み込まれた火炎は輻射熱線化し高率の熱線光波を貫流水管に直照射、或いは反射して熱交換機構が進行し熱交換水は蒸気化が進み圧力弁から噴出する。段落番号００１７、００１８項で高品質の燃料炭化の段階は経過した。
(B) Vaporized gas generated in the tilting furnace is sucked into the boiler connected to the furnace and is burned. The boiler structure is vertical as shown in Fig. 2 and the base furnace is made of steel plate with a furnace wall 15cm thick and a furnace wall inner diameter of 1m with a height of 50cm. There is a temperature detection port in the middle position, and the heat exchange part is 2.5cm in diameter of 2cm high 5cm diameter tube on the lower end square circular diameter tube of 1cm inside diameter and 8cm height and 8cm width on the base furnace. With a steam pressure valve as a steam-water separation chamber by connecting the upper surface with a semicircular square-circumferential pipe with a horizontal width of 8 cm and a height of 25 cm. The outside of the once-through water pipe is surrounded by a steel plate outer wall (5 cm thick) with a far-infrared radiation function furnace wall material and closed with a circular furnace wall plate having a chimney base device having an inner diameter of 20 cm. The chimney base unit is equipped with a chimney diverter, a significant pipe hole at the target position and a temperature detection port at the middle circumferential position, a chimney with sufficient suction power at the top, and a pipe with a significant diameter in the pipe hole Equipped with a high-pressure blower with a check valve at the outside of the furnace, with a right angle descent at the center position of the chimney, a trumpet type high-pressure blower membrane port device with a sharp downward angle is provided at the half of the length of the once-through water pipe, and heat exchange water is at the bottom of the once-through water pipe Supplied by a cascade pump to the circumferential pipe.
When the vaporized gas from the carbonizer is sucked into the boiler by the chimney function with strong suction negative pressure, the burner is injected and the gas is turned into a fire.When the flame is stabilized, the ignition burner is turned off and the high-pressure air blow mechanism in the middle stage of the furnace is activated. A radiant barrier is formed, and the encased flame is converted into radiant heat rays, and a high-rate heat ray light wave is directly applied to the once-through water pipe or reflected, and the heat exchange mechanism proceeds, and the heat exchange water is vaporized and ejected from the pressure valve. . In paragraphs 0017 and 0018, the stage of high-quality fuel carbonization has passed.
（Ｃ）−前項までの手段によって燃料有機体が高品質炭素燃料化されたことを生かしてそれを高率に蒸気にする手段を組立てる。そのボイラー段階は次の仕様による。
ボイラー本体は前項の気化ガス燃焼装置の一周り大きい基部炉壁内径（１．５ｍ）とし基部炉の高さも７５ｃｍ、貫流水管の長さも３．０ｍとし、特にボイラー炉肩から貫流水管下端の炉芯位置まで燃料移送燃焼装置を設置する。その装置は長楕円半円形の断面（底辺３０ｃｍ）の鉄板製で遠赤外線放射機能炉壁を内装し、上端に炭化材燃料供給タンクよりの供給装置を備え、その下端位置で水平開口し、その開口周囲に基部炉床に向けた斜め下方迎角度の一次燃焼用高圧空気噴射膜口パイプを設け、移送装置の上肩を送風管をのばし炉外にチャッキバルブを中継した高圧送風機に継ぐ。熱交換貫流水管関連装置や、二次燃焼用の対向流送風装置、基部炉の着火バーナー等の機器も装具されている。
上述装置の主な起動は、先ず基部炉の着火バーナーが作動し基部炉内壁や、燃料移送燃焼装置や外壁等が充分加熱され、それぞれ炉壁の熱線放射機能域に到達したなら、燃料供給機構が作動しグラファイトに近い燃料が流下しながら炉内外熱で熱せられた装置内の炉壁からの遠赤外線光波と酸欠乾溜機能の相乗機能によって炭素ガスが膨張し高温の一次燃焼空気膜に吸い出されて燃焼反応し火炎が基部炉床に吹き当り反転して上昇し、その一次燃焼炎が安定したら着火バーナーは消され、高温の二次燃焼の対向流高圧送風空気膜が噴射されて輻射バリヤが形成され、包み込まれた二次燃焼炎は輻射熱線化して光波を貫流水管に直照射、或いは反射して熱交換水への熱移転が急速に進み高圧蒸気となって気水分離室の蒸気圧力弁から噴出する。
(C)-Assembling means for converting the fuel organic substance into high-quality carbon fuel by the means up to the preceding paragraph and making it into steam at a high rate. The boiler stage is according to the following specifications.
The boiler body has an inner diameter of the base furnace wall (1.5 m) which is larger than the vaporized gas combustion apparatus in the previous section, the height of the base furnace is 75 cm, and the length of the once-through water pipe is 3.0 m, particularly the furnace at the bottom of the once-through water pipe from the boiler furnace shoulder. Install the fuel transfer combustion device to the wick position. The device is made of an iron plate with an elliptical semicircular cross section (bottom 30 cm) and is equipped with a far-infrared radiation function furnace wall, equipped with a supply device from a carbide fuel supply tank at the upper end, opened horizontally at the lower end position, A high-pressure air injection membrane port pipe for primary combustion at an oblique downward angle of attack toward the base hearth is provided around the opening, and the upper shoulder of the transfer device is extended to a high-pressure blower that extends a blower pipe and relays a check valve outside the furnace. Equipment such as a heat exchange once-through water pipe related device, a counterflow air blower for secondary combustion, and an ignition burner for the base furnace are also equipped.
The main start-up of the above-mentioned device is to start the fuel supply mechanism when the ignition burner of the base furnace is activated and the inner wall of the base furnace, the fuel transfer combustion device, the outer wall, etc. are sufficiently heated and reach the heat ray radiation function area of the furnace wall, respectively. The carbon gas expands due to the synergistic function of the far-infrared light wave from the furnace wall in the equipment heated by the internal and external heat of the furnace while the fuel close to graphite is flowing down and absorbed by the oxygen-depleted dry distillation function, and is absorbed into the high-temperature primary combustion air film The flame burns and reacts to the base hearth and reverses and rises.When the primary combustion flame stabilizes, the ignition burner is turned off, and a countercurrent high-pressure air blown film for high-temperature secondary combustion is injected and radiated. The barrier is formed, and the enclosed secondary combustion flame is converted into radiant heat rays, and light waves are directly applied to the once-through water pipe, or reflected, and the heat transfer to the heat exchange water rapidly proceeds to become high-pressure steam, which becomes the steam in the steam-water separation chamber. It ejects from the steam pressure valve.
（Ｄ）−前項によって効率よく発生した蒸気圧力を活用したベンチュリスクラバ機構によって煙突の排ガスを誘引し高温融合して中圧多量の高温過熱蒸気に変換する技術手段について、本発明者はバイオマスの乾溜ガス化燃焼熱変換発電装置（特願２００４−２０９２４１）によって提案しているが、本願ではその蒸気噴射機構を改良して提案した。通常のベンチュリスクラバ機構は、燃焼促進の為の強制吸引排気の場合や或いは集塵機の供給仕様に高温の排ガスを吸引移動させながら温度を低下させる（３００℃）の為に高圧大量の空気で誘引することが多く、通例、空気吐出口径３と煙道口径１０の断面比は７：７８である。
(D)-Regarding the technical means for attracting the flue gas from the chimney by the venturi scrubber mechanism utilizing the steam pressure generated efficiently according to the preceding paragraph and converting it into high temperature superheated steam with a large amount of medium pressure, the present inventor This is proposed by a gasification combustion heat conversion power generation device (Japanese Patent Application No. 2004-209241). In this application, the steam injection mechanism is improved and proposed. The normal venturi scrubber mechanism is attracted with a large amount of high-pressure air in order to reduce the temperature (300 ° C) while sucking and moving high-temperature exhaust gas in the case of forced suction exhaust to promote combustion or supply specifications of the dust collector In many cases, the sectional ratio of the air discharge port diameter 3 and the
本願における該機構の目的は、高温の煙突排ガス熱（例４００℃）と一次高温強湿り蒸気（例２００℃−１５．８ｋｐ）との両気体の高温融合で更に高温の二次過熱蒸気（例２５０℃−４０．６ｋｐ）とすることを目指すので、両ガス体のみでそれを発象する必要に限定された条件のもとでラッパ型の蒸気噴射機構と膨張圧力緩衝推走機構によってその目的機能に近づくものである。前者は煙突機能管口径１０の拡大された管口径２０の周壁に達する鋭角全周方位噴射口により、管の全断面で吸引する改良タイプで、蒸気拡大吐出断面口径２０と煙道口径１０との断面比は３１４：７８で、４倍の断面で高温排ガスを吸引しながら混合し、融合蒸気化する。後者は融合蒸気の噴射口を包み込む後方全周囲から形成されたハート型空気室によって爆発的（２００℃−２５０℃、１５．８ｋｐ−４０．６ｋｐ）膨張圧力を緩衝して推送圧力に変換して集束された管口から二次過熱蒸気として噴出される。その噴出口は融合蒸気口より拡大され、逆流圧を防ぎながら次につなぐ。
The purpose of the mechanism in the present application is to achieve a higher-temperature secondary superheated steam (eg, a high-temperature fusion of both gases of high-temperature chimney flue gas (eg, 400 ° C.) and primary high-temperature, high-humidity steam (eg, 200 ° C.-15.8 kp)). 250 ° C-40.6 kp), and its purpose is achieved by a trumpet-type steam injection mechanism and an expansion pressure buffer thrust mechanism under conditions limited to the necessity of generating both gas bodies only. It approaches the function. The former is an improved type that sucks in the entire cross section of the pipe by the acute angle omnidirectional injection port reaching the peripheral wall of the expanded
（Ｅ）−蒸気タービンは入口と出口を備えたケーシングに内蔵された、合成正弦曲線を基調とした一次元形状の羽根形と有意の巾を備えた羽根翼複数を偏芯取付配置と側板を組合せた羽根車を、羽根翼外周端を有意にずらして複数並列固定した構成で所要の巾を確保した羽根車で構成され、各羽根翼間はバケット状となる。
回転軸は中空で羽根翼取付部間には羽根入射角度に近い通気孔が開けられている。２次蒸気吐出管口径より広い巾を有するタービンケーシングは、その入口で扁平末広がりとなって高圧蒸気を低圧に膨張させながら有意の角度で羽根に当てる構造で、タービン羽根車は羽根の特性から蒸気の衝動圧力Ｇ点が蒸気の流動慣性と共に移動して途切れることなく回転力価に変換し且偏芯取付配置によりトルクの大きい機能する仕事となる。ケーシングは蒸気滞留外周を有意に保持しているので、回転軸の通気孔からは羽根車の回転によって生ずる負圧に引かれて吸入される冷水によって回転軸が冷却されて軸受を保護し、羽根車の過熱も防ぎながら吐出口で蒸気温度を低下させて容積を縮小させる顕著なマフラー作用を発象して蒸気の流動が促進される。回転による流動慣性をスムーズに保持する羽根形特性は回転抵抗も少なく蒸気の放出も効率よく機能し、又偏芯取付配置による挺子機能も加わって、蒸気圧に比例する回転速度は程々でも蒸気圧力の大部分がトルクの大きい回転力に変換される中圧大容量の蒸気向きタービンである。
(E)-A steam turbine is built in a casing having an inlet and an outlet, and has a one-dimensional blade shape based on a composite sine curve and a plurality of blade blades having a significant width. The combined impeller is constituted by an impeller that secures a required width with a configuration in which a plurality of impeller blade outer peripheral ends are significantly shifted and fixed in parallel, and a bucket shape is formed between the impeller blades.
The rotating shaft is hollow, and a vent hole close to the blade incident angle is opened between the blade blade mounting portions. A turbine casing having a width wider than the diameter of the secondary steam discharge pipe has a structure that spreads flat at the inlet and applies high pressure steam to the blades at a significant angle while expanding to low pressure. The impulse pressure point G moves along with the flow inertia of the steam and is converted into a rotational force value without interruption, and the work with a large torque is performed by the eccentric mounting arrangement. Since the casing retains the steam staying outer periphery significantly, the rotating shaft is cooled by the cold water sucked by the negative pressure generated by the rotation of the impeller from the vent hole of the rotating shaft to protect the bearing, and the blade While preventing overheating of the car, the flow of steam is promoted by generating a remarkable muffler action that reduces the volume of the steam by reducing the steam temperature at the discharge port. The blade-shaped characteristics that smoothly maintain the flow inertia due to rotation have low rotational resistance and function to discharge steam efficiently, and the lever function by the eccentric mounting arrangement is added, so that the rotation speed proportional to the steam pressure is moderate. This is a medium-pressure, large-capacity steam-oriented turbine in which most of the pressure is converted into torque with a large torque.
（Ｆ）−発電装置蒸気タービンの回転力は中速でトルクの大きい特性からそれを生かす発電装置は直径の大きい多極型発電装置を選択する。有意の直径の相対する外輪と内輪相対応の固定子外枠は回転軸を有する回転子内枠の軸受台座に固定され、外枠には多数の固定子が装着され、内枠には多数の回転子が装着されていて、内枠が回転すると固定子群には励起電流と電圧を生じて電気エネルギーとなり、システムの完結となる。
追加々筆すれば、段落番号００１８項のボイラーでの蒸気噴射事象は、チップ供給量を増量する装置においては変換二次過熱蒸気化を経て発電に至る機構に進展し得ることは当然で、炭化装置を移動可能規模とするか、定置大型規模とするかで選択し大型定置装置においては、炭化工程から発電までのシステム完結も可能である。
(F) -Power generation apparatus Since the rotational force of the steam turbine is medium speed and has a large torque, a power generation apparatus that takes advantage of it has a multi-pole power generation apparatus with a large diameter. A stator outer frame corresponding to a significant outer diameter and an inner ring phase is fixed to a bearing pedestal of a rotor inner frame having a rotating shaft, a number of stators are mounted on the outer frame, and a number of stators are mounted on the inner frame. When the rotor is mounted and the inner frame rotates, an excitation current and voltage are generated in the stator group to become electric energy, and the system is completed.
In addition, it is natural that the steam injection event in the boiler of paragraph 0018 can progress to a mechanism that leads to power generation through conversion secondary superheated steaming in a device that increases the amount of chip supply. The system can be completed from the carbonization process to the power generation in the large-sized stationary apparatus, which is selected depending on whether the apparatus is a movable scale or a stationary large-scale apparatus.
総括一順を追って詳述した本願を要約すると、木質系をはじめとするバイオマス有機体は物質の特性上、熱を求めて物体を燃焼するに当っては、原子状炭素と原子状酸素とが燃焼反応してＣＯ2となることが最善の熱源を得られるという文献からの教導を得て、まず燃料として分子状炭素（グラファイト）に進化させることを目指して、炭化処理手段にたどりつき、次の高効率熱交換を目指す貫流水管構成のボイラー炉の内で、炭化斜傾炉構造を小型化した燃料移送燃焼装置でグラファイト燃料を急速に炭素ガス化に進相し、一次燃焼空気膜で吸引燃焼反応し、炉床に当って反転上昇する火炎に二次燃焼対向流送風空気膜によりバリヤ化して包み込まれた一次火炎を輻射熱線化してその二次燃焼炎光波を貫流水管に直照射、反射して熱交換水を一次湿り蒸気化し、圧力弁より噴出するが、本願ではその一次蒸気の噴射圧を活用し改良ベンチュリスクラバ機構を応用して排気ガスを誘引融合して二次過熱蒸気に変換してより高圧の蒸気圧を得て、蒸気タービンを駆動し、その回転力に連動して直径の大きい多極型発動機を作動して発電し、本願システムの目標に到達した。 Summarizing the present application, which has been described in detail in a general order, biomass organisms including woody materials are characterized by the characteristics of substances, and when burning an object for heat, atomic carbon and atomic oxygen are Obtained teaching from the literature that the best heat source can be obtained by combustion reaction to become CO 2 , first aimed to evolve into molecular carbon (graphite) as a fuel, arrived at the carbonization treatment means, the following In a boiler furnace with a once-through water pipe configuration aiming for high-efficiency heat exchange, graphite fuel is rapidly advanced to carbon gasification with a fuel transfer combustion device with a downsized carbonized tilting furnace structure, and suction combustion is performed with a primary combustion air film The primary flame encapsulated by the secondary combustion counterflow blown air film is radiated into a heat ray, and the secondary combustion flame light wave is directly radiated and reflected on the once-through water pipe. Heat exchange water It is converted to secondary superheated steam by converting it into secondary superheated steam by applying the improved venturi scrubber mechanism by utilizing the injection pressure of the primary steam and converting it into secondary superheated steam. The pressure was obtained, the steam turbine was driven, and a multi-pole motor with a large diameter was operated in conjunction with the rotational force to generate power, and the target of the present system was reached.
以上本願システムの手段及び作用について説明したが、それを生かす前提条件について補強する。
（１）．熱交換用の熱を求めて物体の燃焼と炭化等の関連手段を行うに際しては現今の強い加圧送風燃焼方法を避けて、吸引負圧炉環境での燃焼手段に改めることで、大巾な熱源化−輻射熱線化に近づき易く、併せてその光波が直射性であることを生かす熱交換機構装置は格段の熱交換効率を向上し得る。
（２）．熱を求め有機体を燃焼するに際しては、燃焼発熱とは原子状炭素と原子状酸素が反応してＣＯ2ガスとなり発熱するという文献教示をふまえて、そこに至るまで有機体は物質特性上多くの吸熱反応段階を経なければならない宿命にあることを如何にして経過せしめるかに基本的配慮を要することをシステム施行向上の要とすることを忘れてはならない。
Although the means and operation of the system of the present application have been described above, the preconditions for utilizing them will be reinforced.
(1). When performing related measures such as combustion and carbonization of objects in order to obtain heat for heat exchange, avoid the current strong pressurized blast combustion method and replace it with a combustion method in a suction negative pressure furnace environment. A heat exchanging mechanism device that makes it easy to approach heat source-radiant heat radiation and that the light wave is direct radiation can improve remarkably heat exchange efficiency.
(2). Based on the teaching of the literature that when carbon is burned for heat, combustion exotherm is the reaction of atomic carbon and atomic oxygen to generate CO 2 gas and generate heat. It must be remembered that the basic consideration of how to pass the fate that must go through the endothermic reaction stage is the key to improving system implementation.
本願は、発明者が出合った自然現象と文献からの教導の融合によってバイオマス有機体の特性を最大限生かしながら熱源に転換し蒸気に変換し回転力に換えて発電に至るシステムに仕上げ発案した。
今エネルギー資源をめぐる生産と消費課題、地球温暖化問題をめぐる先進国に対比する後進国間との軋轢、産業廃棄物と環境汚染との悪循環、等々地球規模での解決を迫られているやに見受けられるが、研究機関や大企業程、既存技術に固執したやに見える対応で、根元にある技術開発分野では立ち止まっている社会環境にしか見えない。
本発明者は自然現象の出遭いと学術文献の教導との融合によって本システムに進化したものだが、それは劇的と云える燃焼熱源化とその輻射熱線光波の直照射を生かす熱交換機構によって物質の熱転換を熱源まで高め得て広範な技術課題前進に大きく貢献し得ると信じているので、それが生かされることを切に祈っている。
The present application has been conceived as a final design of a system that converts natural phenomena encountered by the inventor and teaching from the literature into the heat source and converts it into steam while making the best use of the characteristics of the biomass organism, and converts it into steam and converts it into rotational force.
Production and consumption issues related to energy resources, conflicts between developing countries compared to developed countries over global warming issues, vicious circle between industrial waste and environmental pollution, etc. However, it seems that research institutions and large companies seem to stick to existing technology, and it seems to be a social environment that has stopped in the underlying technology development field.
The present inventor has evolved into this system by the combination of encountering natural phenomena and teaching of academic literature, but it is based on the heat exchange mechanism that makes the most of the combustion heat source and direct irradiation of radiant heat rays. I believe that it can greatly contribute to the advancement of a wide range of technical issues by raising the heat conversion to the heat source.
本願は多様なバイオマス等有機体を酸欠乾溜炭化した高品質燃料にして、限られた装置内で炭素原子となる解離エネルギーの必要度を最低にして燃料効果を高めたことを出発点として、発熱体に斜め対向流空気膜形成によって高温化するステファン・ボルツマン法則事象を発象させた熱源から相対的直射方法の熱交換を効率化し、得られた蒸気の蒸気圧をも活用する改良されたベンチュリスクラバ機構によって高温の排気ガスを誘引して高温融合転換蒸気に変換して、その中圧大容量の蒸気圧で合成正弦曲線を基調とした羽根形の蒸気タービンで回転力に転換し、そのトルクの大きい回転力で多極型発電機を回して発電するという多段階の機構を組み合わせたシステムに成る。
それぞれの段階の手段を支える機構は自然現象に教えられて開発されたものが多く、その最善の機能向上にはたゆまぬ努力が必要である。例えば炉壁の構成については燃焼化学反応に最適の触媒機能のある輻射熱線の放射力発生源というあまり情報の少ない分野もあり、乾溜、ガス化、燃焼反応に与える熱線光波の影響の大きさが知られて来たからである。それぞれを構成する機器の材質等も同様である。上述技術システムが多段的にわたることからそれに対応できる機構装置の構築の技術面と広範囲にわたる運用現場とを有意に連継して組織化することが決め手となり、併せて事業成果の電気活用分野の開発も急務で、例えば広い山中を移動する装置の電源としてのバッテリー化はまた遠方への一手段ともなる。
The present application is a high-quality fuel obtained by carbonizing various organic organisms such as biomass, and starting from the fact that the fuel effect has been improved by minimizing the need for dissociation energy to become carbon atoms in a limited system. Improved efficiency of heat exchange of the direct direct method from the heat source that generated the Stefan-Boltzmann law phenomenon that is heated by the formation of the diagonal counter-flow air film on the heating element, and also uses the vapor pressure of the resulting steam The venturi scrubber mechanism attracts high-temperature exhaust gas to convert it to high-temperature fusion conversion steam, and its intermediate-pressure large-capacity steam pressure converts it to rotational force with a vane-shaped steam turbine based on a composite sine curve. This system combines a multi-stage mechanism that generates electricity by turning a multi-pole generator with a large torque.
Many of the mechanisms that support the means of each stage have been developed by being taught by natural phenomena, and constant efforts are required to improve their functions. For example, there is a field with very little information on the structure of the furnace wall, such as the radiation source of radiant heat rays that has an optimal catalytic function for combustion chemical reactions, and the magnitude of the influence of heat ray light waves on dry distillation, gasification, and combustion reactions is large. Because it has been known. The same applies to the materials and the like of the devices constituting each. Since the above-mentioned technical system is multi-staged, it is crucial to organize the technical aspects of construction of mechanical devices that can cope with it and a wide range of operation sites, and also develop the electric utilization field of business results. However, there is an urgent need, for example, the use of a battery as a power source for a device that moves in a large mountain is also a means of distant.
以下図面により各段階の手段操作について説明する。
１・ 図1―イ・ロは資材を炭化する傾斜炉で外殻鉄板１と内壁２と下底内壁２〜１が装着されており下底裏下３を耐火レンガで支えられ、バーナー４の燃焼炎に対向流送風膜５を浴びて完全燃焼した排ガスが上昇して通路６から炉内に入りガス移送管７よりの負圧に引かれて下降し、気化ガスと共に図２のボイラーに送られる。資材供給装置８から資材が供給されると無酸素の２次排ガスの熱源とその熱に加熱された上・下の炉壁から発する輻射熱線を浴びながら底面を流下降しながら乾溜炭化されて水冷スクリュー９で排出される。
２． 図２は図１より排出された気化ガスを燃焼熱交換するボイラー装置で、基部炉１１の上に管径の半分の間隙を明けて貫流水管１５を円周形並列し上部は円周角形管で結んで気水分離室１６として圧力弁１７を備え、下端は円周角形下端連結管１２で結んでカスケードポンプ１８で注水する、貫流水管外側は炉壁１４を装着した外殻鉄板１３で囲い上部は煙突２０を備えた円板で閉じ、煙突管には高圧送風機２１を備えた送風管が挿入され直角下降して貫流水管中段高さに炉床に向けた下方迎角度の火炎に向けた高圧送風膜口２２が設けられ、図１からの気化ガスが移送管７を経てガス給入口１０からボイラーに吸入されると着火バーナー１９が作動して気化ガスは火炎となり安定したら着火バーナー１９は消され中段の対向流送風機構が作動して気化ガス炎は輻射熱線化して熱線を貫流水管１５に直照射・反射して貫流水を高温化して蒸気圧力弁１７を押し上げて流出する。これによって図１〜図２の素材酸欠乾溜炭化工程は完了し高品質のグラファイト状炭素素材が集積される。
３． 図３―イはグラファイト状炭素燃料を用いて高率一次蒸気化する装置。基部炉２４の上に管径の半分の間隙を持たせて貫流水管２５が円周並列され下端は円周角形下端連結管２６で結ばれてカスケードポンプ２７を備え、上部は横幅が貫径の１．５倍で高さがその3倍で上部を円形とした円周角形上端連結管２８で結んで気水分離室２９とし圧力バルブ３０を備える。貫流水管外側は炉壁材３１を内装したボイラー外殻鉄板２３で囲い上部は煙突分離部３３を備えた煙突３４を装着した円板３２で閉じ、分離部上方にはダンパー３５を設ける。煙突基部に高圧送風機３６にチャッキバルブ３７で中継したパイプを挿入して煙突中心位置で直角下降し貫流水管中間高さ位置で止め、先端に下方迎角度ラッパ状の高圧空気噴射口管３８を設け２次燃焼炎輻射熱線化装置Ｂとする。
更にボイラー炉肩位置から貫流水管下端炉心位置まで燃料移送燃焼装置Ａを設置する。それは有意の半円形（内壁底面３０ｃｍ×高さ３０ｃｍ）の断面の炉壁材を内装し先端に下方迎角度ラッパ状の高圧空気噴射口管３９を設けるが、上方燃料供給装置４０と高圧の送風機４１と噴射口管をつなぐパイプは本装置の上背に設置する。
４． 図３−ロは上述ボイラーから発生する高圧一次湿り蒸気を受ける二次過熱蒸気変換装置で上述ボイラーの煙突分離部３３より分かれた煙突管４３からの高温排気ガスを図３―イから噴出させる蒸気の圧力を利用して誘引混和して二次過熱蒸気に変換する。蒸気管４４内の蒸気を噴出口４５より拡散噴出すると拡大空気室側壁４６に当たり膜状蒸気は集束して出口に放出される際に生じた負圧に引かれて煙突からの燃焼排ガスである高温のガス体が吸引されるベンチュリスクラバ機構が作動するので噴出源の一次湿り蒸気は高温ガス体とハート型空気室４７内で混合融合されて変換二次過熱蒸気４９に進相し一段と高圧力の蒸気となる。
５． 図４−イ・ハは上述二次過熱蒸気の推進圧力を受けて回転力に変換する機構のタービン装置である。回転室ケーシング５０に内蔵され軸受５１に支えられた中空の回転軸５２と共通の回転軸上の受動回転羽根車５３は、合成正弦曲線羽根形と有意の幅の羽根翼５４の４枚をそれぞれの基部となる円弧接点を回転軸フランジ５５の外周切線に重ね合わせて偏心配置して横板円板に取付けた羽根板複数枚を所要数組み合わせて成ると共に中空の回転軸フランジ５５の壁には羽根翼５４取付け位置に平行的斜めに搾孔されて外気の流通が共通しているので、高圧蒸気圧を有効に回転力に変換できると同時に、羽根翼裏側に生ずる負圧に引かれて回転軸を通して冷水が導入されると軸受５２を保護すると共に放出蒸気を冷却するマフラー機能となり、よりトルクの大きい回転力の維持増強に貢献できる。
６．図４−ロ・ニは上述の蒸気タービンの得られた回転力で駆動して発電する多極型発電装置である。回転室ケーシング５８には内側に多数の固定子５９が装着され、回転軸５２に支えられた内枠６０に多数の回転子６１が固定子５９に相対して装着されている。タービンの回転で内枠６０が回転すると外枠に装着されているは多数の固定子５９に電流と電圧を生じて、大きなエネルギーが得られるという仕様である。
Hereinafter, the means operation at each stage will be described with reference to the drawings.
1. Fig. 1-I Lo is an inclined furnace that carbonizes the material, which is equipped with outer
2. FIG. 2 is a boiler apparatus for exchanging heat of vaporized gas discharged from FIG. 1, and a through water pipe 15 is arranged in a circular shape on the
3. Fig. 3-1 shows a high-rate primary vaporization system using graphite-like carbon fuel. A through
Further, a fuel transfer combustion apparatus A is installed from the boiler furnace shoulder position to the bottom-flow water pipe bottom core position. It has a significant semi-circular (inner wall bottom surface 30 cm ×
4). FIG. 3B is a secondary superheated steam converter that receives the high-pressure primary wet steam generated from the above-mentioned boiler, and steam that ejects the high-temperature exhaust gas from the
5. FIG. 4-i-ha shows a turbine device having a mechanism that receives the propulsion pressure of the secondary superheated steam and converts it into rotational force. A
6). FIG. 4-Roni is a multipolar power generator that generates electric power by driving with the rotational force obtained by the steam turbine described above. A large number of
改めていうまでもなく生産と生活にとって電気なしでは成り立たないことを踏まえた発明者の取り組みは本願までたどり着いた。これから先は発明の効果の項で述べたとおり、世界を上げての課題である産業基盤への貢献対策として特許技術の掘り起こしもその一策ではあるまいか！現在の社会環境は特許技術の活用に対して冷淡ではないかと感じる。
背景技術で述べた通り世界を上げての課題であるエネルギー資源の解決の一翼を担う省エネルギー技術、地球温暖化対策を迫られている資源消費問題、そして環境汚染をももたらす広範囲の産廃資源の解消策等々数えればその必要度は増すばかりに見受けられる。
本願は自然現象との出会いを生かし前述の課題に貢献することを願い複次段階の技術構築に努めて来た。
そして活用の道は単純ではなく、国家的目標を明確に立て、それぞれの段階でそれぞれの立場の関係者、中核となる企業等の有機的組織化によって、資源活用の結果として電気の生産と消費をつなぐ流通経路を構築して、より多くの人々の生活向上につなげて欲しいものである。その可能性は非常に大きいものがあるのではあるまいか！
Needless to say, the inventor's efforts based on the fact that without electricity for production and life have reached the present application. From now on, as described in the section of the effect of the invention, digging up patented technology as a countermeasure to contribute to the industrial base, which is a challenge for raising the world, is one of those measures! I feel that the current social environment is cold to the use of patented technology.
As mentioned in the background art, energy saving technology that plays a part in solving energy resources, which is a challenge for raising the world, resource consumption issues that are required to fight global warming, and elimination of a wide range of industrial waste resources that also cause environmental pollution If you count measures, the need will increase.
This application has been working on the construction of multi-stage technology in the hope of contributing to the above-mentioned problems by making use of encounters with natural phenomena.
And the way of utilization is not simple, and national goals are clearly defined, and the production and consumption of electricity as a result of resource utilization through the organic organization of stakeholders in each position and core companies at each stage. We want you to build a distribution channel that connects people and improve the lives of more people. I don't think there is a very big possibility!
１−外殻鉄板 ２−内壁 ２~１−下底内壁 ３−下底裏下
４−バーナー ５−対向流送風膜 ６−ガス通路 ７−気化ガス移送管 ８−資材供 給装置 ９−水冷スクリュー １０−ガス吸入口 １１―基部炉 １２−円周角形下 端連結管 １３−外殻鉄板 １４−炉壁 １５―貫流水管 １６―気水分離室 １７−蒸気圧力弁 １８−カスケードポンプ １９−着火バーナー ２０−煙突 ２１−高圧送風機 ２２−高圧送風膜口 ２３−ボイラー外殻鉄板 ２４−炉基部 ２５−貫流水管 ２６−円周角形下端連結管 ２７−カスケードポンプ ２８−円周 角形上端連結管 ２９−気水分離室 ３０−圧力バルブ ３１−炉壁材 ３２−円板 ３３−煙突分離部 ３４−煙突 ３５−ダンパー ３６−高圧送風機 ３７−チャッ キバルブ ３８−高圧空気噴射口管 ３９−高圧空気噴射口管 ４０−上方燃料供給 装置 ４１−高圧送風機 ４２−着火バーナー Ａ−燃料移送燃焼装置 Ｂ−２次燃 焼炎輻射熱線化装置 ４３−煙突管 ４４−蒸気管 ４５−噴出口 ４６−拡大空気 室側壁 ４７−ハート型空気室 ４８−温度検知口 ４９−変換二次過熱蒸気 ５０−回転室ケーシング ５１−軸受 ５２−回転軸 ５３−受動回転羽根車 ５４−羽根翼 ５５−回転軸フランジ ５６−高圧蒸気導入口 ５７−蒸気排出口 ５８−発電機ケーシング ５９−固定子 ６０−内枠 ６１−回転子
1-outer iron plate 2-inner wall 2-1-lower bottom inner wall 3-lower bottom back 4-burner 5-counter flow blower film 6-gas passage 7-vaporized gas transfer pipe 8-material supply device 9-water cooling screw 10-gas inlet 11-base furnace 12-circular square lower end connecting pipe 13-outer shell iron plate 14-furnace wall 15-flow-through water pipe 16-gas / water separation chamber 17-steam pressure valve 18-cascade pump 19-ignition burner 20-chimney 21-high pressure blower 22-high pressure blower membrane port 23-boiler shell iron plate 24-furnace base 25-flow-through water pipe 26-circular square lower end connection pipe 27-cascade pump 28-circumferential square upper end connection pipe 29-air Water separation chamber 30-Pressure valve 31-Furnace wall material 32-Disc 33-Chimney separation part 34-Chimney 35-Damper 36-High pressure blower 37-Chuck valve 38-High pressure air injection pipe 39-High pressure air injection pipe 0-Upper fuel supply device 41-High pressure blower 42-Ignition burner A-Fuel transfer combustion device B-2 secondary combustion flame radiant heat line device 43-chimney tube 44-steam tube 45-outlet 46-expanded air chamber side wall 47 -Heart-shaped air chamber 48-Temperature detection port 49-Conversion secondary superheated steam 50-Rotary chamber casing 51-Bearing 52-Rotary shaft 53-Passive rotary impeller 54-Blade blade 55-Rotary shaft flange 56-High-pressure steam inlet 57-Steam outlet 58-Generator casing 59-Stator 60-Inner frame 61-Rotor
Claims (9)
廃棄物的有機体再生のスタートとなる遠赤外線放射機能の炉壁材を内装する傾斜炉でバーナー炎の２次排ガスの無酸素状の熱源により酸欠乾溜炭化してグラファイト状の炭素燃料に改質する手段と、
前記改質の際に生ずる気化ガスをボイラーに誘引して燃焼させる手段と、
前記グラファイト状の炭素状燃料を１次燃焼させる手段と、
前記一次燃焼の炎を炉床に吹き当てて反転上昇させ、中段の下向き高圧対向流送風膜に包み込まれて２次燃焼させる手段と、
前記グラファイト状の炭素状燃料の火炎は輻射熱線化して絶対温度の４乗に比例すると云われる光波に進相して熱交換貫流水管に直照射して高率に熱交換して供給される循環水を急速に一次湿り蒸気に変換して圧力弁より噴出させる手段と、
更にその蒸気圧を活用して煙突の排ガスを吸引するベンチュリスクラバ機能のハート型膨張圧力緩衝装置で二次過熱蒸気に変換させる手段と、
前記二次過熱蒸気を合成正弦曲線羽形の羽根翼の受動回転する蒸気タービン装置で受けて回転力に転換すると共に羽根翼裏側の負圧を活かして中空の回転軸を通して冷水を吸引して軸受を冷やしながら放出蒸気も冷却収縮するマフラー機能を進行させてトルクの大きい回転力に転換させる手段と、
そのトルクの大きな回転力で多極型発電装置を駆動して電気エネルギーを得る手段と、
を有することを特徴とするバイオマス等有機体を重複燃焼熱源化し蒸気変換して発電に至るシステム It is a system that converts organic resources such as biomass into heat sources of overlapping combustion and converts them into steam for power generation ,
A lean furnace equipped with a far-infrared radiation furnace wall material that starts the regeneration of waste-like organisms, and oxygen-depleted carbonized by an oxygen-free heat source of the secondary exhaust gas of the burner flame and modified to a graphite-like carbon fuel Means of quality ,
Means for attracting and burning vaporized gas generated during the reforming to a boiler ;
It means for primary combustion of the graphite-like carbonaceous fuel,
Wherein by blowing upturns abuts have a primary combustion flame to hearth, and means encased in the middle of the downward pressure counter flow blown film to secondary combustion,
The graphite-like carbon-like fuel flame is radiated heat ray and advanced to a light wave that is proportional to the fourth power of the absolute temperature. Means for rapidly converting water into primary wet steam and ejecting it from the pressure valve ;
Furthermore, a means for converting to secondary superheated steam with a heart-shaped expansion pressure buffering device with a venturi scrubber function that draws in the exhaust gas of the chimney utilizing the vapor pressure ,
The secondary superheated steam is received by a passively rotating steam turbine device of a synthetic sinusoidal blade blade and converted into rotational force, and the negative pressure on the back side of the blade blade is utilized to suck in cold water through a hollow rotating shaft to make a bearing. A means of advancing a muffler function that cools and contracts the discharged steam while cooling, and converts it into a torque with a large torque ,
Means for obtaining electric energy by driving the multi-pole power generator with a large rotational force of the torque ;
A system for generating electricity by converting steam and other organic matter such as biomass into a heat source for combustion
（１）ライフグリーン（２）アルミナセメント（３）牡蠣殻焼成石灰を基本としその３種を全て含みそれを目的とする機能構造とする為に（イ）パーム椰子殻成灰（ロ）マリネックス液（ハ）ホウ酸（二）硫酸マンガンの４種全てとを調合反応させて得られた高濃度ホウ酸複合化合液で混練し 分解した外壁鉄板のそれぞれに内装し乾燥した後に 熱線放射型電気炉装置で窒素ガス置換加熱し 熱に反応して遠赤外線光波を発振する機能構造体となることを特徴とする請求項１記載の バイオマス等有機体を重複燃焼熱源化し蒸気変換して発電に至るシステム。The system according to claim 1, wherein waste organic matter is carbonized and converted into steam from combustion and its heat exchange. It is essential that the furnace wall structure of each device has a far-infrared radiation function. the oscillation source and comprising a furnace wall structure (1) Life Green (2) alumina cement (3) oyster shell lime was used as a base (a) palm to the functional structure of its three includes all purposes it Insulated shell ash (b) Marinex liquid (c) Boric acid (2) Mixed with all four types of manganese sulfate and kneaded with the high concentration boric acid composite compound obtained by mixing and reaction The internal combustion and other organic matter such as biomass is burned in an overlapped manner, and after the interior is dried, a functional structure that oscillates far-infrared light waves in response to heat is obtained by heating with nitrogen gas in a heat-radiating electric furnace. Heat source and steam conversion System leading to the power generation Te.
そのボイラー構造仕様の 有意に設定された直径とその半分の高さの円形立型基部炉は遠赤外線放射機能炉壁を内装した鉄板構造で 炭化装置からの気化ガスの移送受入れ口とその対向位置にバーナーを設け その横位置に温度検知口を設け その上部に基部炉の内壁直径と同じ内径列の貫流水管が設けられるが 下部は有意の管直径の１．５倍の横巾と高さの円周形角型管が設けられ その上に基部炉炉壁内径の２倍の高さの水管を、管直径の半分の間隔を設けて円周形並列し その上端は管直径の１．５倍の横巾とその３倍の高さで上面を半円形より成る円周形角型管で結んで気水分離室とし 蒸気圧力バルブを設け 貫流水管への熱交換水は下端の円周形角型管のバルブにカスケードポンプで注入され 貫流水管の外側は 管径の半分の厚さの炉壁素材を内装した鉄板で囲み上面は煙突・基部装置を備えた外壁鉄板で閉じて充分な吸引機能を備えた高さの煙突を装着し 煙突基部装置には煙突分岐口が設けられてダンパーで閉じられ、その対向位置に有意径のパイプ穴が設けられ その直横側にチャッキバルブで中継した高圧送風機を備えたパイプが煙突管内に挿入され煙突径中心位置で直角管で下降し 貫流水管の半分の高さの位置に火炎に向けて対向流送風する下方円形迎角度の高圧空気膜噴射口を設け ボイラーには吸引負炉圧が働きそれに引かれて炭化装置からの気化ガスが移送管から放出されると対向位置のバーナー口からの着火バーナーが点火され ガスは火炎化し 着火した燃焼炎が安定したらバーナーを止め上部の対向流高圧空気膜噴射機構が作動してその高温化した高圧空気膜が対向衝突してバリヤ化し それに包み込まれた火炎は輻射熱線化して光波を貫流水管に直照射 反射して 熱交換水は蒸気に転換し 上部の気水分離室バルブから噴出する機構構造を有することを特徴とする請求項４記載のバイオマス等有機体を重複燃焼熱源化し蒸気変換して発電に至るシステム。 The vaporized gas generated from the carbonization apparatus according to claim 4 is drawn to the negative pressure suction force of the connected boiler and is transferred to the boiler through the gas transfer pipe, but its gas concentration is high, so it is charged and separated from the carbonization furnace to the boiler. A rotary impeller is installed in front of the discharge outlet to prevent back-flow ignition.
The round vertical base furnace with a significantly set diameter and half the height of its boiler structure specification is a steel plate structure with a far infrared radiation function furnace wall, and the gas vapor transfer port from the carbonizer and its opposite position A burner is installed in the horizontal position, a temperature detection port is installed in the horizontal position, and a through-flow water pipe with the same inner diameter column as the inner wall diameter of the base furnace is installed in the upper part, but the lower part has a width and height 1.5 times the significant pipe diameter. A circular square pipe is provided, and a water pipe having a height twice as large as the inner diameter of the base furnace furnace wall is arranged on the circular pipe in parallel with the circumference of the pipe, and the upper end is 1.5 mm of the pipe diameter. A steam pressure valve is provided as a steam-water separation chamber by connecting the upper surface with a semicircular square tube with a double width and three times its height, and a steam pressure valve is provided. It is injected into the valve of the square pipe with a cascade pump, and the outside of the once-through water pipe is a furnace wall element that is half the diameter of the pipe diameter. Top enclosed in interiors and iron plate and is closed by dampers chimney branch port is provided in the mounting and the chimney base apparatus the height of the chimney with a sufficient suction features closed outer wall steel plate having a chimney-base device A pipe hole with a significant diameter is provided at the opposite position, and a pipe equipped with a high-pressure blower relayed by a check valve is inserted directly into the chimney pipe. A high-pressure air film injection port with a downward circular attack angle that blows counter-flow toward the flame is provided at the height position, and the suction negative furnace pressure is applied to the boiler, and vaporized gas from the carbonizer is released from the transfer pipe. Then, the ignition burner from the burner port at the opposite position is ignited, the gas is flamed, and when the ignited combustion flame is stabilized, the burner is stopped and the upper counter-flow high-pressure air film injection mechanism is activated to counteract the high-temperature air film. It was countercurrent collision barrier of encased thereto flame heat exchange water was directly irradiated reflected light waves flow water pipe and the heat ray of morphism congestion is having a mechanism structure ejected from the upper portion of the steam-water separating chamber valve converted to steam The system according to claim 4, wherein the organic substance such as biomass is converted into a heat source for overlapping combustion and converted into steam for power generation.
上述の燃焼と熱交換機構での操作は 先ず着火バーナーが作動し炉内炉壁が充分加熱されて熱線放射機能が保持されると着火バーナーが外され 炉外の燃料供給装置が作動して燃料移送燃焼装置内の燃料が流下しながら炉内高温を受けて熱せられた炉壁からの遠赤外線放射を受けてグラファイト状の分子状炭素燃料は急速に吸熱反応が進行して原子状に近づいてガス化が進み下端の開口部に近づくと 開口周辺の噴出口から噴射される熱せられた高圧空気膜に吸い出されて激しく燃焼反応して燃焼ガスは炉床に当り反転して上昇する１次燃焼反応が進行し それが安定したら中断上部の下向き対向流高圧空気噴射機構が作動し 高温の高圧空気噴射膜と２次燃焼反応して放射バリヤが形成され包み込まれた火炎の軸射熱線化ガスの光波を貫流水管に直照射 反射する２次燃焼熱交換反応が進行し その光波を受けた貫流水管内の循環水は効率よく熱に反応して蒸気化し蒸気圧力弁を押し上げて噴出する機能構造を有することを特徴とする請求項４または５記載のバイオマス等有機体を重複燃焼熱源化し蒸気変換して発電に至るシステム。 In response to the fact that the biomass such as biomass can be reformed to a fuel body close to inorganic graphite by the carbonization apparatus according to claim 4 or 5, the next combustion means and the efficient combustion means are obtained for the next stage heat source conversion. Combined with the heat exchange means device, it is converted into steam. The boiler body of the mechanism conforms to the structure of the boiler of the carbonizer , but the diameter of the large-sized one is 1.5 times , the height of the base furnace is also half the diameter, and the height of the flow-through water pipe with a significant pipe diameter is also twice the diameter. The mechanism is equipped with an inclined fuel transfer device up to the core position of the once-through water pipe, but it is made of iron plate structure with a significant semicircular cross section, and the inner wall is equipped with far-infrared radiation function furnace wall material and the bottom is carbonized fuel The bottom is horizontally open and the lower end is horizontally open, and a primary combustion air injection port circular tube with a downward angle of attack is provided around it, and a high pressure is relayed through a check valve outside the furnace through the blower tube at the top of the transfer device. A set of fuel supply devices are connected to the combustion transfer device outside the furnace connected to the blower, and a set of high-pressure air blowing mechanisms equipped with a high-pressure air injection port for secondary combustion are installed at the center of the once-through water pipe.
The above-described combustion and heat exchange mechanism operations are as follows. First, when the ignition burner is activated and the furnace wall is sufficiently heated to maintain the heat radiation function, the ignition burner is removed and the fuel supply system outside the furnace is activated to operate the fuel. The graphite-like molecular carbon fuel rapidly undergoes an endothermic reaction due to the far-infrared radiation from the furnace wall heated by the high temperature in the furnace while the fuel in the transfer combustion apparatus flows down and approaches the atomic state When gasification progresses and approaches the opening at the lower end, it is sucked out by the heated high-pressure air film injected from the jet outlet around the opening and burns violently. The combustion gas hits the hearth and reverses and rises. When the combustion reaction progresses and stabilizes, the downward counter flow high-pressure air injection mechanism operates at the upper part of the interruption, and a secondary combustion reaction with the high-temperature high-pressure air injection film forms a radiation barrier and is encapsulated in the flame. The light wave of Circulating water of the irradiation reflected secondary combustion heat exchange reaction is subjected to the light wave progresses through-flow water pipe is characterized by having a function structure for ejecting pushes up the steam pressure valve vaporized in response to heat efficiently system leading to power generation with steam converting duplicate combustion heat of the claims 4 or 5 such as biomass organisms according.
蒸気パイプ先端の噴出装置からラッパ型膜状に高圧力の高温蒸気が射放出されると拡大されたハート型空気室側壁にあたり膜状蒸気は集束して出口に放出される際に生じた負圧に引かれて煙管からの燃焼排ガスである高温のガス体が吸引されるベンチュリスクラバ機能が作動するので射出源の一次湿り蒸気は煙突から吸引された高温ガス体とハート型空気室内で混合融合されて変換二次過熱蒸気に進相し一段と高圧力の蒸気となる機構構造を有することを特徴とする請求項１記載の バイオマス等有機体を重複燃焼熱源化し蒸気変換して発電に至るシステム。 The next device aiming at further secondary superheated steam conversion by converting the primary wet steam generated with high efficiency in the efficient combustion and heat exchange device is the chimney base installed on the top outer wall steel plate top of the large boiler mentioned above Stop the horizontal smoke pipe connected to the chimney diverter provided sideways of the device at a position set at a right angle downward at a significant position with the main body, and simultaneously insert the steam pipe connected to the steam pressure valve into the smoke pipe. When the smoke pipe center position descends at a right angle and stops at the lower end of the smoke pipe, a trumpet-type steam injection device with an acute omnidirectional direction that reaches the peripheral wall of the smoke pipe whose diameter is expanded by several percent in the direction of combustion exhaust gas is installed at the pipe tip At the same time, the outer smoke pipe wraps around it, forming a heart-shaped air chamber around the rear, and its tip is focused on a 20% larger diameter pipe than the base smoke pipe to function as an expansion pressure buffering transmission mechanism that becomes a secondary conversion steam discharge pipe Next Transition to become.
When high-pressure high-temperature steam is sprayed and released in the form of a trumpet-type film from the jet device at the tip of the steam pipe, the negative pressure generated when the film-like steam converges and is discharged to the outlet when hitting the expanded heart-shaped air chamber side wall The venturi scrubber function that draws the high-temperature gas body, which is the combustion exhaust gas from the smoke pipe, is activated and the primary wet steam from the injection source is mixed and fused in the heart-shaped air chamber with the high-temperature gas body sucked from the chimney. The system according to claim 1, wherein the system has a mechanism structure in which the converted secondary superheated steam is advanced into a higher pressure steam, and the biomass such as biomass is converted into a heat source for overlapping combustion and converted into steam for power generation.
前述の機構構成のもとで強圧蒸気が導入されると羽根車の羽根翼は 蒸気の導入受けから排出されるまでその受動点（Ｇ）を移動させながら蒸気圧力を受け止め トルクの大きい回転力に転換すると共に 併せてその流動慣性によって羽根翼裏面に生ずる負圧に引かれる冷水吸入が機能して、回転軸受けを冷やしながら 吐出蒸気を冷却し容積を収縮するマフラー機能に進相する二重の機能構成であることを特徴とする請求項１記載の バイオマス等有機体を重複燃焼熱源化し蒸気変換して発電に至るシステム。 The steam turbine mechanism that receives high-temperature steam pressure, which is the converted secondary superheated steam generated by the secondary superheated steam conversion device, is built in a casing that has an open steam receiving part and a discharge part. A rotating impeller integrated with a shaft rotates in response to a passive impact thrust generated by strong external pressure steam, and converts the steam pressure into rotational force. A rotating flange with a hollow structure with a set diameter of a plurality of blade blades with a sine curve composed of a sine curve of a selected amplitude and range and a wing shape with an effective inside of a primary shape. The base arc contact is overlapped with the outer peripheral cutting line of the rotating shaft flange selected at a specific position, and it is eccentrically arranged and attached. The impeller plural sets to render homogeneous the rotational force to ensure the necessary width in combination as to Distribute blade outer circumferential blade edge on its finish circumference, further rotation shaft flange through the hollow of the rotary shaft Circulation of outside air is common, and the flange wall near the blade blade mounting position is squeezed diagonally parallel to the blade blade, and it is a mechanism that draws cold water by being drawn by the negative pressure generated on the back surface due to rotation .
When high-pressure steam is introduced under the above-described mechanism configuration, the impeller blade blades receive the steam pressure while moving its passive point (G) until it is discharged from the steam introduction receptacle, and the torque is increased. In addition to the conversion, the cold water suction drawn by the negative pressure generated on the back of the blade blades due to the flow inertia functions, and the dual function to advance to the muffler function that cools the discharged steam and shrinks the volume while cooling the rotary bearing The system according to claim 1, wherein an organic material such as biomass is converted into a heat source for overlapping combustion and converted into steam to generate power.
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| CN106287748A (en) * | 2016-08-26 | 2017-01-04 | 合肥合意环保科技工程有限公司 | A kind of dangerous waste incinerator complexes |
| CN106352341A (en) * | 2016-08-26 | 2017-01-25 | 合肥合意环保科技工程有限公司 | Combustion generation method and combustion equipment of waste |
| CN113881461A (en) * | 2021-09-28 | 2022-01-04 | 兖矿新疆煤化工有限公司 | Method for rapidly replacing process burner of gasification furnace |
| CN117346146A (en) * | 2023-12-04 | 2024-01-05 | 山西三水能源股份有限公司 | Biomass auxiliary type garbage pyrolysis equipment |
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| JP7208607B2 (en) * | 2019-05-09 | 2023-01-19 | 株式会社環健スーパーテクノ | Incinerator |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN106287748A (en) * | 2016-08-26 | 2017-01-04 | 合肥合意环保科技工程有限公司 | A kind of dangerous waste incinerator complexes |
| CN106352341A (en) * | 2016-08-26 | 2017-01-25 | 合肥合意环保科技工程有限公司 | Combustion generation method and combustion equipment of waste |
| CN113881461A (en) * | 2021-09-28 | 2022-01-04 | 兖矿新疆煤化工有限公司 | Method for rapidly replacing process burner of gasification furnace |
| CN117346146A (en) * | 2023-12-04 | 2024-01-05 | 山西三水能源股份有限公司 | Biomass auxiliary type garbage pyrolysis equipment |
| CN117346146B (en) * | 2023-12-04 | 2024-02-13 | 山西三水能源股份有限公司 | Biomass auxiliary type garbage pyrolysis equipment |
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