JPH08120287A - Molded fuel, and process and apparatus for producing same - Google Patents

Molded fuel, and process and apparatus for producing same

Info

Publication number
JPH08120287A
JPH08120287A JP25669794A JP25669794A JPH08120287A JP H08120287 A JPH08120287 A JP H08120287A JP 25669794 A JP25669794 A JP 25669794A JP 25669794 A JP25669794 A JP 25669794A JP H08120287 A JPH08120287 A JP H08120287A
Authority
JP
Japan
Prior art keywords
algae
powder
coal
power plant
shell
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP25669794A
Other languages
Japanese (ja)
Other versions
JP3028498B2 (en
Inventor
Masabumi Matsumoto
正文 松本
Yoshiharu Fukuju
芳治 福寿
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsui Engineering and Shipbuilding Co Ltd
Original Assignee
Mitsui Engineering and Shipbuilding Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsui Engineering and Shipbuilding Co Ltd filed Critical Mitsui Engineering and Shipbuilding Co Ltd
Priority to JP6256697A priority Critical patent/JP3028498B2/en
Publication of JPH08120287A publication Critical patent/JPH08120287A/en
Application granted granted Critical
Publication of JP3028498B2 publication Critical patent/JP3028498B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE: To obtain a molded fuel which enables the effective utilization of waste materials and contributes to the protection of the global environment by using a shell powder and algae obtainable in the neighborhood of a thermal power plant. CONSTITUTION: The molded fuel contains a coal powder, a shall powder as a desulfurizing agent, and algae, is produced by mixing a coal powder, a shell powder obtd. by subjecting shells collected in the neighborhood of a thermal power plant to aerobic fermentation to decompose and eliminate org. substances, and cultured algae obtd. by fixing CO2 contained in the exhaust gas of the plant to algae by photosynthesis, and is pref. a mixture comprising 40-75wt.% coal powder, 5-20wt.% shell powder, and 10-40wt.% algae (on dry basis). A coal powder of 50-200 mesh, a shell powder of 50-200 mesh, and dehydrated algae as such are used. Shells discarded in culturing, food processing, eating, etc., can also be used.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は火力発電所周辺で調達で
きる原料を使用し、かつ廃棄物を有効利用すると同時に
地球環境の保全にも貢献できる成形体燃料およびその製
造法、および該成形体燃料の製造装置に関する。より詳
しくは本発明は石炭を原料とし、脱硫剤として貝殻粉末
を使用し、排ガス中のCO2 を藻類の光合成により固定
化して得られる培養藻類を使用した成形体燃料、その製
造法および製造装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a molded body fuel that uses raw materials that can be procured in the vicinity of a thermal power plant, can effectively use waste, and at the same time contributes to preservation of the global environment, a method for producing the same, and a molded body. The present invention relates to a fuel manufacturing device. More specifically, the present invention uses a coal as a raw material, uses shell powder as a desulfurizing agent, and uses molded algae obtained by immobilizing CO 2 in exhaust gas by photosynthesis of algae, a molded body fuel, a manufacturing method and a manufacturing apparatus thereof. Regarding

【0002】[0002]

【従来の技術】世界のエネルギー使用量は近年益々増大
してきており、エネルギー源の枯渇が近未来の問題とし
てクローズアップされてきている。このような状況か
ら、最近燃料としての石炭の利用価値が見直され、石炭
の粉末や、スラリーおよびブリケットの形態の石炭燃料
が火力発電用燃焼炉や焼却炉で使用されてきている。
2. Description of the Related Art The amount of energy used in the world has been increasing more and more in recent years, and the depletion of energy sources has been highlighted as a problem in the near future. Under such circumstances, the utility value of coal as a fuel has recently been reviewed, and coal powder, coal fuel in the form of slurry and briquette have been used in combustion furnaces for thermal power generation and incinerators.

【0003】それと同時に環境汚染の問題も大きくとり
あげられるようになってきており、石炭燃焼排ガス中に
含まれるSO2 による環境汚染やCO2 による地球温暖
化が世界的に問題となり、それらの大気中への排出抑制
および排出量規制が現実の課題となっている。このよう
なエネルギー問題と環境問題とを同時に解決するため、
石炭に木材カスや藁などの植物質を加えて燃焼性を改善
し、およびさらに脱硫剤として消石灰を加え、さらに粘
結剤として糖蜜を混合した複合固形燃料は既に公開され
ている(特開平6−80974号公報)。また、炭素質
燃料に、脱硫剤としての消石灰や炭酸カルシウム等、お
よび低温時の脱硫剤としてアンモニウム化合物を混合し
た固形燃料も開示されている(特開平5−105889
号公報)。
At the same time, the problem of environmental pollution has come to be widely taken up, and environmental pollution due to SO 2 contained in coal combustion exhaust gas and global warming due to CO 2 have become a global problem, and they have become a problem in the atmosphere. Emissions control and emission control are becoming real issues. To solve such energy problems and environmental problems at the same time,
A composite solid fuel in which plant materials such as wood debris and straw are added to coal to improve combustibility, and slaked lime is further added as a desulfurizing agent, and molasses is further mixed as a binding agent has been already disclosed (Japanese Patent Laid-Open No. 6-58242). -80974). Also disclosed is a solid fuel in which carbonaceous fuel is mixed with slaked lime or calcium carbonate as a desulfurizing agent and an ammonium compound as a desulfurizing agent at low temperature (Japanese Patent Laid-Open No. 105889/1993).
Issue).

【0004】[0004]

【発明が解決しようとする課題】しかし石炭に混合され
る木材、藁、バガスなどの植物質は地域性、時期、定常
的入荷などに問題があり、収集コストを無視できない。
また、石炭中には石油よりはるかに多量の硫黄が含有さ
れているので、燃焼排ガス中に多量の硫黄酸化物が生成
し、これらによる環境汚染を防止するための脱硫剤とし
て従来法では消石灰、炭酸カルシウムなどが石炭原料に
添加するかもしくは炉内に投下されている。しかし、脱
硫剤の消費量が多いためそのコストが無視できないもの
となっており、また適当な形状例えばブリケットに成型
するための粘結剤として添加されるコーンスターチ、糖
蜜、タール、重質油、等も製造コストを押し上げてい
る。
However, plant materials such as wood, straw, and bagasse mixed with coal have problems in locality, time, and regular arrival, and the collection cost cannot be ignored.
In addition, since coal contains much more sulfur than petroleum than petroleum, a large amount of sulfur oxide is generated in the combustion exhaust gas, and slaked lime is used in the conventional method as a desulfurizing agent for preventing environmental pollution due to these, Calcium carbonate or the like is added to the coal raw material or is dropped in the furnace. However, the cost of the desulfurizing agent is so high that it cannot be ignored, and cornstarch, molasses, tar, heavy oil, etc., which is added as a binder for forming a suitable shape such as a briquette, are also available. Is also pushing up manufacturing costs.

【0005】ところで、火力発電所の冷却水取水口や排
出口周辺に種々の貝類が付着し、特に取水口周辺では冷
却水の取り込みを妨害したり、発電機の故障原因となる
ため定期的に採取し廃棄されている貝類が埋め立て処理
されたり、廃棄物業者に廃棄料金を払ってただ廃棄物と
して処分されているという事実がある。この廃棄物から
は運搬時に悪臭を放ち、水が滴り、周辺住民の苦情のも
とになっている。また埋め立て処理するにしても処理場
に余力はなく、いずれは発電所内で自己完結的に処理す
ることを考えねばならない状態となっていた。
By the way, various shellfish adhere to the cooling water intake and outlet of the thermal power plant, especially around the intake because they interfere with the intake of the cooling water and cause a failure of the generator. There is the fact that the shellfish that are collected and discarded are either landfilled or are simply disposed of as waste by paying a disposal fee to the waste disposal companies. This waste gives off a foul odor during transportation and drips water, which is a source of complaints from the local residents. In addition, even if the landfill treatment is carried out, there is no surplus in the treatment site, and eventually it was necessary to consider self-contained treatment within the power plant.

【0006】本発明者らはこの貝殻の約75%が炭酸カ
ルシウムであるという事実に着目した。この貝類を廃棄
せず脱硫剤として有効利用できればゴミ処理問題を解決
できると同時に有望な炭酸カルシウム源にもなる。ま
た、近年地球温暖化防止の観点から排ガス中の炭酸ガス
をできるだけ低減させることが課題となっており、炭酸
ガスの総量規制が実施されるのは時間の問題となってい
る。従って炭酸ガスを除去するための種々の方法が世界
的規模で研究されており、なかでも、炭酸ガスは植物の
光合成により固定化されて酸素に変換されること、およ
び藻類は森林のおよそ10倍の炭酸ガス固定能力を有す
ることから、藻類に光合成させて排ガス中の炭酸ガスを
固定化除去する方法が炭酸ガスの効果的除去法の一つと
してほぼ確立されている。
The present inventors have noted the fact that about 75% of this shell is calcium carbonate. If this shellfish can be effectively used as a desulfurizing agent without being discarded, it can solve the waste disposal problem and at the same time become a promising calcium carbonate source. Further, in recent years, from the viewpoint of prevention of global warming, it has been a subject to reduce carbon dioxide gas in exhaust gas as much as possible, and it is a matter of time before the total amount of carbon dioxide gas is regulated. Therefore, various methods for removing carbon dioxide are being researched on a global scale. Among them, carbon dioxide is fixed by photosynthesis in plants and converted into oxygen, and algae are about 10 times as much as forests. Since it has the ability to fix carbon dioxide, the method of fixing carbon dioxide in exhaust gas by photosynthesis by algae is almost established as one of the effective methods of removing carbon dioxide.

【0007】しかし、光合成による固定化方法は、炭酸
ガス除去法としては効果的でも、例えば50万キロワッ
トの火力発電所の場合で数千トンもの培養藻類がバイオ
マスとして得られ、今度は藻類の処分に困るという事態
を招いていた。これら培養藻類の処理法が種々検討され
たが、焼却によるのがコスト的には最も有利であること
が判明している。しかしただ焼却するのでは炭酸ガスの
低減という意図と矛盾するので、何か好都合な処理方法
が模索されていた。
However, although the immobilization method by photosynthesis is effective as a carbon dioxide removal method, for example, in the case of a thermal power plant of 500,000 kilowatts, thousands of tons of cultured algae can be obtained as biomass, and this time the algae disposal I was in trouble. Various treatment methods for these cultured algae have been studied, but it has been found that incineration is the most advantageous in terms of cost. However, since incineration is inconsistent with the intention of reducing carbon dioxide, some convenient treatment method was sought.

【0008】本発明者らはこの光合成培養により生成す
るバイオマスが好都合なことに乾燥重量あたり50%の
炭素を含有する有力な燃料源でありかつ着火性に優れて
いるという事実に着目した。着火性に優れていることは
低温域での石炭の未燃炭素の発生を抑制できるため、石
炭の助燃剤として使用できる。しかも藻類は炭素質に加
え糖やタンパク質を含有していて藻類それ自体が粘結剤
としても役立つこともコスト削減に寄与できよう。
The present inventors have noted the fact that the biomass produced by this photosynthetic culture is conveniently a powerful fuel source containing 50% carbon per dry weight and is excellent in ignitability. The excellent ignitability can suppress the generation of unburned carbon of coal in a low temperature range, and thus can be used as a combustion improver for coal. Moreover, since algae contain sugars and proteins in addition to carbonaceous material, the algae themselves can also serve as a binder, which may contribute to cost reduction.

【0009】もしここで、前記回収貝殻中に含有される
炭酸カルシウムを脱硫剤として活用し、藻類の光合成に
よって得られた培養藻類を助燃剤とし、これらを火力発
電所で容易に入手できる石炭と混合して燃料に成形すれ
ば、すべて火力発電所およびその周辺という同一サイト
で容易に入手できる原料から性能のよい燃料を製造で
き、その上脱硫剤および助燃剤それ自体のコストも低減
できることを見出した。特に集中排気源である火力発電
所周辺での公害防止および環境対策を自己完結型のサイ
クルで達成でき、しかも廃棄物の回収再利用と資源の有
効活用を図れる点で産業上高い有用性を有する。
If the calcium carbonate contained in the recovered shell is utilized as a desulfurizing agent, the cultured algae obtained by photosynthesis of algae are used as a combustion improver, and these are used as coal easily available at a thermal power plant. It was found that if mixed and molded into fuel, it is possible to produce a high-performance fuel from raw materials that are easily available at the same site of the thermal power plant and its periphery, and also reduce the cost of the desulfurizing agent and the combustion improver itself. It was In particular, it has high industrial utility in that it can achieve pollution prevention and environmental measures in the vicinity of a thermal power plant, which is a central exhaust source, in a self-contained cycle, and also can collect and reuse waste and effectively use resources. .

【0010】[0010]

【課題を解決するための手段】それ故本発明は、石炭粉
末と、脱硫剤としての貝殻粉末と、藻類とを含有する成
形体燃料を提供する。特に、前記貝殻粉末が火力発電所
取水口および/または排水口周辺から採取された貝類を
好気性発酵させ有機物を分解除去して得られた貝殻の粉
末であり、前記藻類が火力発電所の排ガス中のCO2
藻類に光合成固定化させることにより得られた培養藻類
である前記成形体燃料が好ましい。脱硫剤として貝殻粉
末を使用した例はこれまで存在しない。
SUMMARY OF THE INVENTION The present invention therefore provides a green fuel containing coal powder, shell powder as a desulfurizing agent, and algae. In particular, the shell powder is a shell powder obtained by aerobically fermenting shellfish collected from around the intake and / or drain of a thermal power plant to decompose and remove organic matter, and the algae are exhaust gas from the thermal power plant. The molded body fuel, which is a cultured alga obtained by photosynthetically immobilizing CO 2 in the alga, is preferable. Until now, there has been no example of using shell powder as a desulfurizing agent.

【0011】本発明はさらに、石炭粉末と、火力発電所
周辺から採取された貝類を好気性発酵させ有機物を分解
除去して得られた貝殻の粉末と、火力発電所の排ガス中
のCO2 を藻類に光合成固定化させることにより得られ
た培養藻類とを混合し成形する、成形体燃料の製造法を
も提供する。本発明では前記貝殻粉末は火力発電所以外
の大規模工場取水口および/または排水口周辺で回収さ
れる貝類、その他養殖、食品加工、食事等で廃棄された
貝殻の粉末をも含有できる。また前記藻類に加え、それ
以外の植物質例えば木質系物質の粉砕物も含有できる。
The present invention further includes coal powder, shell powder obtained by aerobically fermenting shellfish collected from the periphery of a thermal power plant to decompose and remove organic matter, and CO 2 in exhaust gas of the thermal power plant. Also provided is a method for producing a molded body fuel, which comprises mixing with a cultured algae obtained by immobilizing algae on photosynthesis and molding the mixture. In the present invention, the shell powder may also contain shellfish powder collected around the intake and / or drain of large-scale factories other than thermal power plants, and other shell powder discarded in aquaculture, food processing, meals and the like. In addition to the algae, other plant matter, for example, a pulverized product of a wood-based substance can be contained.

【0012】本発明はまた前記した成形体燃料を製造す
るための装置にも関する。すなわち本発明は、石炭粉砕
装置と、回収貝を好気発酵させる装置と、発酵装置から
貝殻を回収する装置と、該回収された貝殻の粉砕装置
と、藻類の光合成バイオリアクター装置と、培養藻類を
分離する装置とを備え、前記石炭粉砕装置からの粉末
と、前記貝殻の粉砕装置からの貝殻粉末と、前記分離さ
れた培養藻類とを混合する混合装置と、該混合装置から
の混合物を成形する成形装置とを含む成形体燃料の製造
装置にも関する。
The invention also relates to a device for producing the above-mentioned shaped body fuel. That is, the present invention is a coal crushing device, a device for aerobically fermenting recovered shellfish, a device for recovering shells from the fermentation device, a device for crushing the recovered shell, a photosynthetic bioreactor device for algae, and cultured algae. A mixing device for mixing the powder from the coal crushing device, the shell powder from the shell crushing device, and the separated cultured algae, and a mixture from the mixing device. The present invention also relates to an apparatus for producing a molded body fuel, including the forming apparatus for

【0013】本発明による成形体燃料に含有される藻類
は、炭素質に加え糖やタンパク質、さらには幾分かの水
分も含有しており、従って藻類それ自体が助燃剤である
と同時に粘結剤として役立ち、別途粘結剤を添加する必
要がなくコスト削減に寄与できる。以下、本発明をより
詳細に説明する。
The algae contained in the molded fuel according to the present invention contains not only carbonaceous matter but also sugars, proteins and some water, so that the algae itself is a combustion improver and also a caking agent. It serves as an agent and can contribute to cost reduction without the need to add a binder separately. Hereinafter, the present invention will be described in more detail.

【0014】本発明による成形体燃料は石炭粉末を40
〜75重量%好ましくは55〜65重量%、前記脱硫剤
を5〜20重量%好ましくは8〜12重量%、そして前
記培養藻類を乾燥物として10〜40重量%好ましくは
15〜30重量%含有するような割合で混合するのが好
適である。本発明により使用される前記石炭粉末は50
〜200メッシュ、好ましくは80〜150メッシュ、
特に100メッシュ前後が好ましい。また貝殻粉末は5
0〜200メッシュ、好ましくは80〜150メッシ
ュ、特に100メッシュ前後であり、そして前記藻類は
それ自体が微細なので特に粉砕せずとも脱水しさえすれ
ばそのままでも充分使用できる。
The green fuel according to the present invention comprises coal powder of 40%.
-75 wt%, preferably 55-65 wt%, the desulfurizing agent 5-20 wt%, preferably 8-12 wt%, and the cultured algae as a dried product 10-40 wt%, preferably 15-30 wt% It is preferable to mix them at a ratio such that The coal powder used according to the present invention is 50
~ 200 mesh, preferably 80-150 mesh,
Particularly, about 100 mesh is preferable. Also, the shell powder is 5
It is 0 to 200 mesh, preferably 80 to 150 mesh, especially around 100 mesh, and since the algae are fine themselves, they can be sufficiently used as they are as long as they are dehydrated without crushing.

【0015】石炭は火力発電所の石炭ヤードに野積みさ
れたものを粉砕後、混合装置に投入すればよい。粉砕機
としてはボールミル型例えば転動ボールミル、振動ボー
ルミル、遊星ミル、あるいは攪拌ミル型例えばスクリュ
ー型等任意の適当な石炭用粉砕機を使用すれば良い。転
動ボールミルが最も好ましい。脱硫剤の原料となる貝類
は、火力発電所の冷却水取水口および排水口周辺の壁、
柵等に付着する貝類であり、例えば、ふじつぼ類、ほや
類、ムラサキイガイ等の軟体動物類などがあげられる。
最も一般的で多量に採取されるものはムラサキイガイで
ある。これらには通常身が付着しており、貝殻のみを分
離して乾燥粉砕して使用するのが好ましいが、少量の身
が付着したままでも乾燥後粉砕して使用することができ
る。
The coal may be loaded in a mixing device after crushing coal loaded in a coal yard of a thermal power plant. As the pulverizer, any suitable coal pulverizer such as a ball mill type such as a rolling ball mill, a vibrating ball mill, a planetary mill, or a stirring mill type such as a screw type may be used. Rolling ball mills are most preferred. The shellfish, which is the raw material of the desulfurization agent, is the wall around the cooling water intake and drain of the thermal power plant,
Shellfish attached to fences and the like, and examples thereof include barnacles, husks, mollusks such as blue mussels, and the like.
The most common and large-scale collection is the mussel. Usually, the body is attached to these, and it is preferable to separate and dry only the shells for use, but it is also possible to use after pulverizing after drying even with a small amount of the body attached.

【0016】貝殻から身を除去して貝殻のみを回収する
には、貝類を洗浄して付着した砂等をほぼ除去したの
ち、湿式好気性発酵により有機物を分解除去する。湿式
好気性発酵は連続式または回分式で操作でき、円筒型、
箱型等の発酵槽中で、種々の菌、例えばバクテリアとし
てバチルス(Bacillus)、ズーグロエア(Zoogloea)、カ
ンジダ(Candida)、およびシュードモナス(Pseudomona
s )、そして繊毛虫類としてボルチセラ(Vorticella)
、オペルクラリア(Opercularia)などの1種以上を含
有する発酵液中に浸漬し、大気圧下、空気通気量0.01〜
1vvm、温度15〜45℃、通常は室温で、約2週間から
2か月間、通常1か月間発酵させる。
In order to remove the body from the shell and recover only the shell, the shells are washed to remove almost any attached sand and the like, and then organic matter is decomposed and removed by wet aerobic fermentation. Wet aerobic fermentation can be operated continuously or batchwise, cylindrical type,
In a fermenter such as a box type, various bacteria such as Bacillus, Zoogloea, Candida, and Pseudomonas as bacteria.
s), and as a ciliate, Vorticella
, Opelcularia (Opercularia), etc., soaked in a fermented liquor containing at least one of them, and atmospheric aeration of 0.01 ~
Fermentation is carried out at 1 vvm, temperature 15-45 ° C., usually room temperature for about 2 weeks to 2 months, usually 1 month.

【0017】発酵終了後は有機質である身が溶解消失
し、ほぼ貝殻のみが残るのでこれを発酵装置から取り出
して水切りし、場合により100〜200℃で熱風乾燥
後、所定の粉末度に粉砕したのち混合装置に投入する。
熱風乾燥には発電所の余熱を利用すればよく、新たなエ
ネルギーを必要としない。貝殻の粉砕にはボールミル型
例えば転動ボールミル、振動ボールミル、遊星ミル、あ
るいは攪拌ミル型例えばスクリュー型等の、石炭の粉砕
にあげられたと同様の粉砕機を適宜使用でき、転動ボー
ルミルが好ましい。
After the fermentation is completed, the organic substance dissolves and disappears, and almost only the shell remains. Therefore, the shell is taken out from the fermenter, drained, optionally dried with hot air at 100 to 200 ° C., and then ground to a predetermined fineness. Then add to the mixing device.
The hot air drying may use the residual heat of the power plant and does not require new energy. For crushing shells, a ball mill type such as a rolling ball mill, a vibrating ball mill, a planetary mill, or a stirring mill type such as a screw type mill can be used as appropriate, and the rolling ball mill is preferable.

【0018】水切り後の発酵液中には発酵菌が残存する
ので捨てないで循環再使用するかまたは後述する光合成
バイオリアクター反応槽に導入し、環境中に放流する水
分量を低減させることができる。また湿式好気性発酵槽
からの排気は臭気が強いので、脱臭装置を通して排気し
てもよいが、この排気は炭酸ガスを含有するので光合成
バイオリアクター反応槽に導入して炭酸ガスを浄化し同
時に脱臭したのち排気した方が好都合である。
Since the fermenting bacteria remain in the fermented liquid after draining, it can be recycled without being discarded or introduced into the photosynthetic bioreactor reaction tank described later to reduce the amount of water released into the environment. . Also, since the exhaust from the wet aerobic fermentation tank has a strong odor, it may be exhausted through a deodorizing device, but since this exhaust contains carbon dioxide, it is introduced into the photosynthetic bioreactor reaction tank to purify the carbon dioxide and simultaneously deodorize it. After that, it is more convenient to exhaust.

【0019】こうして得られた貝殻粉末には炭酸カルシ
ウムが約75%含まれる他リン、カリウム等も含まれる
が、それらを分離精製することなく貝殻粉末全体をその
まま脱硫剤として使用できる。脱硫剤として貝殻粉末を
使用するのは本発明が初めてであり、安価に原料を入手
できること、しかも廃棄物を有効利用できることは当業
者にとっても予想外であり、価値ある発明である。
The shell powder thus obtained contains about 75% calcium carbonate and also phosphorus, potassium and the like, but the whole shell powder can be used as it is as a desulfurizing agent without separating and purifying them. The present invention is the first time that the shell powder is used as the desulfurizing agent, and it is an unexpected and valuable invention for those skilled in the art that the raw material can be obtained at low cost and the waste can be effectively used.

【0020】脱硫剤としては前記した貝殻粉末に加え、
他の回収貝類、養殖、食品加工、食事等の際に廃棄され
る貝殻の粉末も使用できる。従って貝類の産地で身を取
り出した後の、大量に廃棄される貝殻の処分にも貢献で
きる。本発明の成形体燃料における藻類には種々のもの
が使用可能であるが、火力発電所の排ガス中のCO2
藻類に光合成固定化させることにより得られた培養藻類
が好ましい。前記光合成とは植物が二酸化炭素と水から
光の存在下に炭水化物を合成する反応を指す。本発明の
成形体燃料の製造法において光合成に使用できる藻類を
あげれば、入手容易で取扱容易で、しかも乾燥すれば特
に粉砕操作せずともそのまま使用できる微細藻類、例え
ば2〜10ミクロンの寸法のものが好ましく、具体的に
は藍藻のスピルリナ、緑藻のクロレラ、等があげられ
る。緑藻クロレラが好ましい。
As a desulfurizing agent, in addition to the above-mentioned shell powder,
Other recovered shellfish, shell powder that is discarded during aquaculture, food processing, meals, etc. can also be used. Therefore, it can also contribute to the disposal of a large amount of shells that are discarded after they are taken out from the shellfish production area. Although various kinds of algae can be used in the molded fuel of the present invention, cultured algae obtained by photosynthetically immobilizing CO 2 in the exhaust gas of a thermal power plant to algae are preferable. The photosynthesis refers to a reaction in which a plant synthesizes a carbohydrate from carbon dioxide and water in the presence of light. Examples of algae that can be used for photosynthesis in the method for producing a molded body fuel of the present invention include microalgae that are easily available and easy to handle, and can be used as they are without being particularly pulverized if dried, for example, having a size of 2 to 10 microns. Preferred are, for example, cyanobacterium Spirulina, green alga Chlorella, and the like. The green alga Chlorella is preferred.

【0021】藻類の光合成装置は、藻類が光合成できる
装置であれば種類を問わないが、光を装置内部まで浸透
せしめることのできる内部照射型の光ファイバー導入型
光合成バイオリアクターが好ましい。光合成バイオリア
クターの形状は円筒型、箱型、等任意のものでよく、バ
イオリアクター装置の下方から排ガスを導入しCO2
吸収させる。CO2 吸収率が低い場合はバイオリアクタ
ー装置からの排気をリアクター装置に戻して再循環させ
ることによりCO2 吸収率をさらに高めることができ
る。
The photosynthetic apparatus for algae may be of any type as long as it can photosynthesize algae, but an internal irradiation type optical fiber introduction type photosynthetic bioreactor capable of allowing light to penetrate into the apparatus is preferable. The photosynthetic bioreactor may have any shape such as a cylindrical shape or a box shape, and exhaust gas is introduced from below the bioreactor device to absorb CO 2 . When the CO 2 absorption rate is low, the CO 2 absorption rate can be further increased by returning the exhaust gas from the bioreactor device to the reactor device and recirculating it.

【0022】藻類はバイオリアクター中で適切な濃度、
好ましくは0.5〜2.0g/Lの濃度に懸濁させる。
火力発電所からの排ガスはCO2 濃度が20%前後であ
り、温度が60℃前後であるのでバイオリアクターに導
入した場合に程よい温度をもたらし、藻類によるCO2
の固定に好適に使用できる。光合成条件としては、大気
圧下、排ガス通気量0.01〜1vvmで、太陽光およ
び、例えばメタルハライドランプ、キセノンランプ、蛍
光灯のような人工光(100〜1000μE/m2 s)を
使用し、バイオリアクター内部への光の導入は石英ガラ
スまたはプラスチック製の光ファイバーを使用すればよ
い。培養温度10〜60℃、好ましくは20〜40℃で
光合成培養により増殖させる。培養温度は排ガスの余熱
によりもたらされる熱分で十分に賄えるので、新たなエ
ネルギーを必要としない。
The algae have a suitable concentration in the bioreactor,
It is preferably suspended at a concentration of 0.5 to 2.0 g / L.
Exhaust gas from a thermal power plant has a CO 2 concentration of around 20% and a temperature of around 60 ° C., so when introduced into a bioreactor, it produces a moderate temperature, and CO 2 due to algae
It can be suitably used for fixing. As the photosynthesis conditions, under atmospheric pressure, exhaust gas ventilation of 0.01 to 1 vvm, using sunlight and artificial light (100 to 1000 μE / m 2 s) such as a metal halide lamp, a xenon lamp, and a fluorescent lamp, Light can be introduced into the bioreactor by using an optical fiber made of quartz glass or plastic. It is grown by photosynthetic culture at a culture temperature of 10 to 60 ° C, preferably 20 to 40 ° C. Since the culture temperature can be sufficiently covered by the heat content produced by the residual heat of the exhaust gas, new energy is not required.

【0023】増殖した藻類はバイオリアクターから適宜
継続的または断続的に取り出し、分離装置で培養母液と
分離脱水し、藻類に混入した培養液中の塩分を除去する
ため数回洗浄水を加えては脱水する操作を繰り返したの
ち、最終的に含水率20〜70%、好ましくは40〜6
0%程度となるまで脱水する。このものは成形体燃料の
製造にほどよい水分を含有するのでそのまま混合装置に
導入できるが、場合により100〜200℃の熱風で乾
燥し、さらに所定の粉末度に粉砕したのち混合装置に導
入することもできる。熱風乾燥には発電所の余熱を利用
すればよく、新たなエネルギーを必要としない。
The grown algae are continuously or intermittently taken out from the bioreactor as appropriate, separated and dehydrated from the culture mother liquor by a separator, and washing water is added several times in order to remove salt in the culture broth mixed with the algae. After repeating the dehydration operation, the final water content is 20 to 70%, preferably 40 to 6
Dehydrate to 0%. This product can be introduced into the mixing device as it is because it contains water that is suitable for the production of molded fuel, but in some cases it is dried with hot air of 100 to 200 ° C., further pulverized to a predetermined fineness, and then introduced into the mixing device. You can also The hot air drying may use the residual heat of the power plant and does not require new energy.

【0024】培養藻類の分離機としては、遠心分離式、
フィルタープレス型等、種々使用でき、遠心分離式が好
都合である。藻類を分離後の母液は光合成バイオリアク
ターまたは湿式好気発酵装置に循環再使用できる。バイ
オリアクターは継続運転できるので、ひとたび運転を開
始したら自動操作により長期間運転できる。こうして得
られた藻類は乾燥重量あたり約50%の炭素を含有し、
炭素源として役立つのみならず、500〜700℃とい
う低温領域での炉内着火性を高めることができるので、
石炭が不完全燃焼して未燃焼炭素が生成するのを阻止で
きる助燃剤であると同時に、成形体となすための粘結剤
としても有用である。
As a separator for cultured algae, a centrifugal separation type,
Various types such as a filter press type can be used, and a centrifugal separation type is convenient. The mother liquor after the separation of algae can be recycled and reused in a photosynthetic bioreactor or a wet aerobic fermenter. Since the bioreactor can be operated continuously, once started, it can be operated for a long time by automatic operation. The algae thus obtained contain about 50% carbon by dry weight,
Not only can it serve as a carbon source, but it can enhance the in-furnace ignitability in the low temperature range of 500 to 700 ° C.
It is a combustion improver that can prevent the incomplete combustion of coal and generation of unburned carbon, and is also useful as a binder for forming a molded body.

【0025】本発明における成形体燃料には、藻類の他
にも間伐材や木質系粗大ゴミのような木質系物質の粉砕
物をも含有することができる。上記のようにして得られ
た石炭粉末、脱硫剤、および培養藻類を任意の順序で混
合装置に投入して混合し、次にこの混合物を当業上慣用
に使用される通常の成形装置、例えば大塚鉄工製K14
4型または高圧ブリケット製造装置に導入して温度20
〜100℃、好ましくは40〜80℃で1〜4t/cm2
の圧力の下に成型し、適当な形状となす。成形体燃料の
形状は、燃料としての使用目的および取扱の容易さなど
からみて長さ20〜50mm×20〜50mm、厚み20
mm程度の顆粒やブリケットがよく、40×35×20mm
程度の顆粒状が好適である。
In addition to algae, the molded fuel of the present invention can also contain pulverized products of wood-based substances such as thinned wood and wood-based coarse dust. The coal powder obtained as described above, the desulfurizing agent, and the cultured algae are put into a mixing device in any order and mixed, and then the mixture is mixed with a conventional molding device conventionally used in the art, for example, Otsuka Iron Works K14
It is installed in a type 4 or high-pressure briquette manufacturing machine and the temperature is 20
~ 100 ° C, preferably 1 ~ 4t / cm 2 at 40 ~ 80 ° C
Mold under pressure to form a proper shape. The shape of the molded fuel has a length of 20 to 50 mm × 20 to 50 mm and a thickness of 20 in view of the purpose of use as a fuel and the ease of handling.
Granules or briquettes of about mm are good, 40 × 35 × 20 mm
A granular form is suitable.

【0026】[0026]

【実施例】【Example】

実施例1 本発明の成形体燃料の製造工程および装置の1例を示す
図1のフローチャートにより、本発明をさらに説明す
る。石炭を転動型ボールミル中で100メッシュに粉砕
した。
Example 1 The present invention will be further described with reference to the flow chart of FIG. 1 showing an example of the manufacturing process and apparatus of the molded body fuel of the present invention. Coal was ground to 100 mesh in a rolling ball mill.

【0027】これと別に、発電所取水口および排水口周
辺からロボットを用いて回収した付着貝を洗浄槽1で洗
浄後、バクテリアとしてバチルス(Bacillus)、ズーグ
ロエア(Zoogloea)、カンジダ(Candida)、およびシュー
ドモナス(Pseudomonas )、そして繊毛虫類としてボル
チセラ(Vorticella) 、オペルクラリア(Opercularia)
の混合物を含有する培養液1m3 を含む箱型の空気導入
式開放型湿式好気発酵装置2(容量1.5m3 )にスク
リューコンベア3Aで供給した。発酵液温を30℃前後
に保持し、送風機から1.0vvmの通気量で空気を導
入しながら大気圧下好気的に発酵させた。1か月後には
繊維状物質がわずかに残るのみで、貝の身がほぼ溶解消
失した。貝殻をスクリューコンベア3Bで水洗/水切り
コンベア4に移して洗浄、水切りし、転動式ボールミル
粉砕機5中で100メッシュに粉砕した。水切り水受槽
12で回収された発酵液は湿式好気発酵装置2あるいは
光合成バイオリアクター6に循環して再利用した。
Separately from this, after the attached shells collected by a robot from around the intake and drain of the power plant are washed in the washing tank 1, as bacteria, Bacillus, Zoogloea, Candida, and Pseudomonas, and as ciliates Vorticella, Opercularia
The mixture was fed to a box-shaped air-introduced open wet aerobic fermentation apparatus 2 (capacity 1.5 m 3 ) containing 1 m 3 of the culture solution containing the mixture of 3 ) by a screw conveyor 3A. Fermentation liquid temperature was maintained around 30 ° C., and aerobically fermented under atmospheric pressure while introducing air from a blower at an air flow rate of 1.0 vvm. After one month, only a small amount of fibrous material remained, and the shellfish were almost dissolved and disappeared. The shells were transferred to the water washing / draining conveyor 4 by the screw conveyor 3B, washed, drained, and pulverized to 100 mesh in the rolling ball mill pulverizer 5. The fermented liquid collected in the drainage water receiving tank 12 was circulated to the wet aerobic fermentation device 2 or the photosynthetic bioreactor 6 for reuse.

【0028】集光装置7およびプレート状(30mm×
10mm×60mm)のプラスチック製内部照射用光フ
ァイバー照射板8を備えた光合成バイオリアクター6
(処理量一日当たりCO2 200g/m3 )中に、緑藻
クロレラを1.0g/Lの濃度に懸濁させた培養液(5
0リットル)を充填し、火力発電所からの排ガス(温度
約60℃、CO2 約20%含有)を、通気量0.5vv
mで導入した。液温は排ガスのもつ温度のためほぼ25
〜30℃に保たれた。このバイオリアクターに昼間は太
陽光を導入し、夜間や曇りの場合は蛍光灯(100〜1
000μE/m2s)および太陽光と蛍光灯を併用し、
大気圧下で光合成させた。
Light collecting device 7 and plate shape (30 mm ×
Photosynthesis bioreactor 6 equipped with plastic optical fiber irradiation plate 8 for internal irradiation (10 mm × 60 mm)
A culture solution (5% CO 2 per day of CO 2 200 g / m 3 ) in which green alga Chlorella was suspended at a concentration of 1.0 g / L (5
0 liter), and the exhaust gas from the thermal power plant (temperature of about 60 ° C., containing about 20% of CO 2 ) has an air flow rate of 0.5 vv.
Introduced in m. The liquid temperature is about 25 due to the temperature of the exhaust gas.
It was kept at ~ 30 ° C. Sunlight is introduced into this bioreactor during the day and fluorescent lights (100-1
000 μE / m 2 s) and using sunlight and fluorescent light together,
Photosynthesis was performed under atmospheric pressure.

【0029】クロレラの濃度を経時的に観察し、約2.
5g/Lを越えたらリアクターから内容物を毎時0.6
Lで取り出し、遠心分離式脱水機9で培養液と培養藻類
とを分離すると同時に水洗を数回繰り返し、含水率50
%となるまで脱水した。バイオリアクター上方から排出
される排ガスはなおCO2 を約19%含有しており、バ
イオリアクターに再循環させた。
The concentration of chlorella was observed with time, and about 2.
If it exceeds 5 g / L, the content of the reactor is 0.6 per hour.
L is taken out, and the culture solution and the cultured algae are separated by a centrifugal dehydrator 9, and at the same time, water washing is repeated several times to obtain a water content of 50.
It was dehydrated until it became a percentage. Exhaust gas discharged from the bioreactor above still has a CO 2 contained about 19%, it was recycled to the bioreactor.

【0030】前記粉砕石炭65重量部、貝殻粉砕物10
重量部、および培養クロレラ25重量部を混合装置10
に導入し、よく混合したのち全量を大塚鉄工製高圧ブリ
ケット装置11に供給し、およそ60℃の温度で2.5
トン/cm2 の圧力の下、40×40×20mmの顆粒
状のブリケット成形体となした。こうして得られたブリ
ケット成形体を、脱硫剤として水酸化カルシウムを含有
する従来法固形燃料と比較して燃焼実験を行い、得られ
た灰中の硫黄分を分析して固定化硫黄量を比較した。従
来法固形燃料はCa/Sモル比1〜2で固定化率が60
〜80%であったのに対し、本発明のブリケット成形体
は同じモル比で固定化率75〜85%を示した。これは
貝殻の主成分である炭酸カルシウムの他に、貝殻に含有
されている微量の金属成分が硫黄分の固定化促進効果を
及ぼしたものと考えられる。 実施例2 円筒状の湿式好気発酵装置(容量150リットル)を使
用し、身が消失後の貝殻を回収後、乾燥機中150〜1
60℃で30〜45分間熱風乾燥し、そして培養藻類を
分離後140〜160℃で30分間熱風乾燥し転動式ボ
ールミルで100メッシュに粉砕する以外は実施例1に
おけると同様にして操作した。実施例1におけると同様
の成形体燃料が得られた。
65 parts by weight of the crushed coal, 10 crushed shells
Mixing unit 10 parts by weight and 25 parts by weight of culture chlorella
Introduced into the high temperature briquette device 11 made by Otsuka Tekko Co., Ltd.
Under a pressure of ton / cm 2 , a granulated briquette compact of 40 × 40 × 20 mm was formed. The briquette compact thus obtained was subjected to a combustion experiment by comparing it with a conventional solid fuel containing calcium hydroxide as a desulfurizing agent, and the sulfur content in the obtained ash was analyzed to compare the immobilized sulfur content. . Conventional solid fuel has a Ca / S molar ratio of 1-2 and an immobilization rate of 60.
˜80%, whereas the briquette compact of the present invention showed an immobilization rate of 75 to 85% at the same molar ratio. It is considered that this is because, in addition to calcium carbonate, which is the main component of the shell, a trace amount of metal components contained in the shell exerted an effect of promoting the immobilization of sulfur content. Example 2 Using a cylindrical wet aerobic fermenter (capacity 150 liters), after collecting shells after disappearance of the body, 150-1 in a dryer
The same procedure as in Example 1 was carried out except that hot-air drying was carried out at 60 ° C. for 30 to 45 minutes, and after the cultured algae were separated, hot-air drying was carried out at 140 to 160 ° C. for 30 minutes and pulverized to 100 mesh by a tumbling ball mill. A molded fuel similar to that in Example 1 was obtained.

【0031】[0031]

【発明の効果】火力発電所周辺で従来はただ廃棄処分さ
れていた貝殻を脱硫剤として有効利用してコスト削減を
はかると同時に亜硫酸ガスの発生を阻止できる。また、
地球温暖化をもたらす排ガス中の炭酸ガスを光合成によ
り固定化除去して浄化すると同時に藻類を培養し、得ら
れた培養藻類をブリケット燃料の炭素源かつ助燃剤かつ
粘結剤として使用でき、地球温暖化の防止および燃料製
造コスト削減に寄与できる。従って火力発電所およびそ
の周辺という同一サイトで容易に調達可能な材料から、
自己完結型のプロセスで価値の高い成形体燃料を提供で
き、同時に公害防止と環境破壊防止を図ることができ
る。
EFFECTS OF THE INVENTION By using shells that have been conventionally disposed of in the vicinity of a thermal power plant as a desulfurizing agent, it is possible to reduce costs and prevent the generation of sulfurous acid gas. Also,
Carbon dioxide in the exhaust gas that causes global warming is fixed and removed by photosynthesis to purify it, and at the same time, algae are cultured, and the obtained cultured algae can be used as a carbon source of briquette fuel, as a combustion improver, and as a binder. It can contribute to prevention of fuel consumption and reduction of fuel production cost. Therefore, from materials that can be easily procured at the same site, the thermal power plant and its surroundings,
A self-contained process can provide a high-value molded fuel, and at the same time can prevent pollution and environmental damage.

【図面の簡単な説明】[Brief description of drawings]

【図1】成形体燃料の製造工程のフローチャートの一例
を示す。
FIG. 1 shows an example of a flowchart of a process for producing a molded body fuel.

【符号の説明】[Explanation of symbols]

1 貝洗浄槽 2 湿式好気発酵
装置 4 洗浄/水切りコンベア 5 粉砕機 6 光合成バイオリアクター 7 光ファイバー
照射板 9 分離装置 11 高圧ブリケッ
ト装置 M モータ
1 Shell Wash Tank 2 Wet Aerobic Fermenter 4 Washing / Draining Conveyor 5 Crusher 6 Photosynthetic Bioreactor 7 Optical Fiber Irradiation Plate 9 Separation Device 11 High Pressure Briquette Device M Motor

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 石炭粉末と、脱硫剤としての貝殻粉末
と、藻類とを含有する成形体燃料。
1. A molded fuel containing coal powder, shell powder as a desulfurizing agent, and algae.
【請求項2】 石炭粉末と、火力発電所周辺から採取さ
れた貝類を好気性発酵させ有機物を分解除去して得られ
た貝殻の粉末と、火力発電所の排ガス中のCO2 を藻類
に光合成固定化させることにより得られた培養藻類とを
混合し成形する、成形体燃料の製造法。
2. Coal powder and shell powder obtained by aerobically fermenting shellfish collected from around the thermal power plant to decompose and remove organic matter, and CO 2 in the exhaust gas of the thermal power plant are photosynthesized to algae. A method for producing a molded fuel, which comprises mixing and molding the cultured algae obtained by immobilization.
【請求項3】 石炭粉砕装置と、回収貝を好気発酵させ
る装置と、発酵装置から貝殻を回収する装置と、該回収
された貝殻の粉砕装置と、藻類の光合成バイオリアクタ
ー装置と、培養藻類を分離する装置とを備え、前記石炭
粉砕装置からの粉末と、前記貝殻の粉砕装置からの貝殻
粉末と、前記分離された培養藻類とを混合する混合装置
と、該混合装置からの混合物を成形する成形装置とを含
む成形体燃料の製造装置。
3. A coal crushing device, a device for aerobically fermenting recovered shellfish, a device for recovering shells from the fermentation device, a device for crushing the recovered shells, a photosynthetic bioreactor device for algae, and cultured algae. A mixing device for mixing the powder from the coal crushing device, the shell powder from the shell crushing device, and the separated cultured algae, and a mixture from the mixing device. And an apparatus for manufacturing a molded body fuel.
JP6256697A 1994-10-21 1994-10-21 Molded fuel, method of manufacturing the same, and manufacturing apparatus Expired - Fee Related JP3028498B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6256697A JP3028498B2 (en) 1994-10-21 1994-10-21 Molded fuel, method of manufacturing the same, and manufacturing apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6256697A JP3028498B2 (en) 1994-10-21 1994-10-21 Molded fuel, method of manufacturing the same, and manufacturing apparatus

Publications (2)

Publication Number Publication Date
JPH08120287A true JPH08120287A (en) 1996-05-14
JP3028498B2 JP3028498B2 (en) 2000-04-04

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ID=17296226

Family Applications (1)

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Country Status (1)

Country Link
JP (1) JP3028498B2 (en)

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JP2008170104A (en) * 2007-01-12 2008-07-24 Chugoku Electric Power Co Inc:The Method of inhibiting elution of harmful trace element utilizing organic waste
JP2009536528A (en) * 2006-05-10 2009-10-15 オハイオ・ユニバーシテイ Apparatus and method for growing biological organisms for fuel and other purposes
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Publication number Priority date Publication date Assignee Title
US10465121B2 (en) 2013-11-20 2019-11-05 Nelson Mandela Metropolitan University Processing carbonaceous materials

Cited By (6)

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Publication number Priority date Publication date Assignee Title
JP2009536528A (en) * 2006-05-10 2009-10-15 オハイオ・ユニバーシテイ Apparatus and method for growing biological organisms for fuel and other purposes
JP4887423B2 (en) * 2006-05-10 2012-02-29 オハイオ・ユニバーシテイ Apparatus and method for growing biological organisms for fuel and other purposes
JP2008170104A (en) * 2007-01-12 2008-07-24 Chugoku Electric Power Co Inc:The Method of inhibiting elution of harmful trace element utilizing organic waste
JP4726810B2 (en) * 2007-01-12 2011-07-20 中国電力株式会社 Method for suppressing elution of harmful trace elements or their compounds using organic waste
JP2018530324A (en) * 2015-06-10 2018-10-18 ブリサ インターナショナル リミテッド ライアビリティー カンパニー Biomass breeding method and system, and treatment plant
JP2022088392A (en) * 2015-06-10 2022-06-14 ブリサ インターナショナル リミテッド ライアビリティー カンパニー System and method for biomass growth and processing

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