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JP2886644B2 - How to recycle carbon dioxide - Google Patents
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JP2886644B2 - How to recycle carbon dioxide - Google Patents

How to recycle carbon dioxide

Info

Publication number
JP2886644B2
JP2886644B2 JP2228443A JP22844390A JP2886644B2 JP 2886644 B2 JP2886644 B2 JP 2886644B2 JP 2228443 A JP2228443 A JP 2228443A JP 22844390 A JP22844390 A JP 22844390A JP 2886644 B2 JP2886644 B2 JP 2886644B2
Authority
JP
Japan
Prior art keywords
carbon dioxide
microalgae
carbonaceous
fuel
waste gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP2228443A
Other languages
Japanese (ja)
Other versions
JPH04110395A (en
Inventor
信行 西川
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.)
Tokyo Electric Power Co Holdings Inc
Original Assignee
Tokyo Electric Power Co Inc
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 Tokyo Electric Power Co Inc filed Critical Tokyo Electric Power Co Inc
Priority to JP2228443A priority Critical patent/JP2886644B2/en
Publication of JPH04110395A publication Critical patent/JPH04110395A/en
Application granted granted Critical
Publication of JP2886644B2 publication Critical patent/JP2886644B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/151Reduction of greenhouse gas [GHG] emissions, e.g. CO2

Landscapes

  • Physical Or Chemical Processes And Apparatus (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Liquid Carbonaceous Fuels (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Treating Waste Gases (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、炭酸ガスの回収と再利用が効率よく行える
炭酸ガスのリサイクル方法、それにより得られる直接燃
焼可能な低コストの炭素質燃料および当該燃料の一成分
を形成する微細藻類の生産方法に関する。
The present invention relates to a carbon dioxide gas recycling method capable of efficiently recovering and reusing carbon dioxide gas, a direct-combustible low-cost carbonaceous fuel obtained by the method, and The present invention relates to a method for producing microalgae that forms one component of the fuel.

〔従来の技術〕[Conventional technology]

近年、地球温暖化等の環境保全の見地から、石炭、石
油等の化石燃料を使用する燃焼炉から排出される廃ガス
中の炭酸ガスの処理が問題になってきた。NOx、SOxにつ
いては有効な回収方法が開発されて一応満足できる成果
が得られているが、炭酸ガスについては満足できる回収
方法が現在まだ得られていない。
In recent years, from the viewpoint of environmental conservation such as global warming, the treatment of carbon dioxide in waste gas discharged from a combustion furnace using fossil fuels such as coal and petroleum has become a problem. Although effective recovery methods have been developed for NOx and SOx, satisfactory results have been obtained, but no satisfactory recovery method for carbon dioxide has been obtained yet.

地球上で行われている炭酸ガスの固定は、そのほとん
ど全部の量が、緑色植物の光合成によっていることは周
知の事実であり、しかもそのうちの大部分は、海水中に
存在する植物性プランクトンと称する微細藻類が行って
いることも知られている。ところで、クロレラやセネデ
スムスのような藻体1kgを生産するのに炭酸ガス約1.7kg
を光合成減量として必要とし、使用炭酸ガスの利用率を
50%の高率と仮定しても約3.4kgの炭酸ガスを必要とす
ることも知られている(有機合成化学、第34巻第5号20
頁、1976年)。
It is a well-known fact that almost all the carbon dioxide fixation performed on the earth is due to photosynthesis of green plants, and most of it is due to phytoplankton existing in seawater. It is also known that the named microalgae are performing. By the way, to produce 1 kg of algal bodies like Chlorella and Senedesmus, about 1.7 kg of carbon dioxide gas
Is required as photosynthetic weight loss, and the utilization rate of
It is also known that about 3.4 kg of carbon dioxide gas is required even at a high rate of 50% (Organic Synthetic Chemistry, Vol. 34 No. 5, No. 20)
P. 1976).

〔発明が解決しようとする課題〕[Problems to be solved by the invention]

発酵工場、セメント工場、製鉄工場、火力発電所等の
廃ガスは数%以上の炭酸ガスを含んでいる。しかもそれ
らの量は膨大で、火力発電所だけでも、我が国だけで年
間約5、700万トンの炭素が大気中に排気されている。
Waste gas from fermentation factories, cement factories, steel plants, thermal power plants, etc. contains more than a few percent of carbon dioxide. Moreover, their volume is enormous, and even thermal power plants alone emit about 57 million tons of carbon into the atmosphere annually in Japan alone.

本発明の目的はこの膨大な量の炭酸ガスを効率よく回
収し、再利用することにある。
An object of the present invention is to efficiently collect and reuse this huge amount of carbon dioxide gas.

〔課題を解決するための手段〕[Means for solving the problem]

本発明者は炭酸ガスの回収及びその再利用について鋭
意研究を行った結果、炭酸ガスを有効に利用する方法を
見い出し、本発明を完成するに至った。
As a result of intensive studies on the recovery and reuse of carbon dioxide gas, the present inventors have found a method of effectively using carbon dioxide gas, and have completed the present invention.

すなわち、本発明の第1の発明は、炭酸ガス含有廃ガ
スを発生する火力発電所等の工場に微細藻類培養池を併
設し、当該廃ガスから炭酸ガス分離器により、又はアミ
ンへの吸収若しくはゼオライトへの吸着により炭酸ガス
を分離し、当該分離した炭酸ガスを、光合成を利用して
微細藻類に固定し、得られる微細藻類を粉砕してそのま
ま或いは微粉炭水スラリーや重油等の炭酸質燃料に添加
して燃料として再度、火力発電所等の工場へリサイクル
させることを特徴とする炭酸ガスのリサイクル方法にあ
る。
That is, the first invention of the present invention is to install a microalgae cultivation pond in a plant such as a thermal power plant that generates carbon dioxide-containing waste gas, and to separate the waste gas from the waste gas by a carbon dioxide separator, Carbon dioxide gas is separated by adsorption to zeolite, the separated carbon dioxide gas is fixed to microalgae using photosynthesis, and the obtained microalgae is pulverized as it is or a carbonaceous fuel such as fine coal water slurry or heavy oil. And recycling it again as a fuel to a plant such as a thermal power plant.

また、本発明の第2の発明は、次の成分、すなわち 以下の(A)若しくは(B)の組成物又は(C)の混
合物に、前記リサイクル方法により生産した微細藻類が
添加された、微細藻類含有炭素質燃料である。
Further, a second invention of the present invention provides a method for preparing a fine algae, wherein the microalgae produced by the recycling method is added to the following components, ie, the following composition (A) or (B) or a mixture of (C): Algae-containing carbonaceous fuel.

(A)(a)石炭、オイルコークス、石油ピッチ系など
の炭素質固体粉末、 (b)少なくとも1種の分散剤、 (c)少なくとも1種の安定化剤及び (d)水 を主成分とする炭素質固体・水スラリー組成物 (B)重油などの炭素質液体組成物 (C)上記(A)の炭素質固体・水スラリー組成物と上
記(B)の炭素質液体組成物との混合物 また、本発明の第3の発明は、燃焼廃ガスから分離し
た炭酸ガスと光照射により微細藻類を生産することを特
徴とする微細藻類の生産方法に係るものである。
(A) (a) carbonaceous solid powder such as coal, oil coke, petroleum pitch, (b) at least one dispersant, (c) at least one stabilizer, and (d) water as a main component. (B) Carbonaceous liquid composition such as heavy oil (C) A mixture of the above (A) carbonaceous solid / water slurry composition and the above (B) carbonaceous liquid composition A third invention of the present invention relates to a method for producing microalgae, which comprises producing microalgae by irradiating light with carbon dioxide gas separated from combustion waste gas.

分散剤としては、ナフタリンもしくはクレオソート油
のスルホン化物、それらの塩またはこれらの脂肪族アル
デヒド付加縮合物、あるいはスルホン酸基含有アミノト
リアジンの脂肪族アルデヒド縮合生成物またはこれらの
塩が挙げられる。
Examples of the dispersant include a sulfonated product of naphthalene or creosote oil, a salt thereof or an aliphatic aldehyde addition condensate thereof, or a sulfonic acid group-containing aminotriazine condensation product of an aliphatic aldehyde or a salt thereof.

また安定化剤としては、粘土鉱物、特に、モンモリロ
族または/およびキサンタンガムが好ましいが、カオリ
ン族、イライト族なども使用できる。
As the stabilizer, clay minerals, in particular, montmorillo and / or xanthan gum are preferable, but kaolin and illite can also be used.

〔実施例〕〔Example〕

以下、本発明を実施例により具体的に説明する。但
し、本発明は、これら実施例により限定されるものでは
ない。
Hereinafter, the present invention will be described specifically with reference to examples. However, the present invention is not limited by these examples.

〔実施例1〕 以下、本発明の炭酸ガスのリサイクル方法を第1図の
概念図により説明する。
Embodiment 1 Hereinafter, a method for recycling carbon dioxide gas according to the present invention will be described with reference to the conceptual diagram of FIG.

火力発電所から発生する多量の炭酸ガス含有廃ガスは
炭酸ガス分離器に供給されて炭酸ガスや他のガスに分離
される。分離された炭酸ガスは直接または一度液化炭酸
ガスとして貯蔵された後微細藻類培養槽に供給される。
この培養槽で炭酸ガスと光照射により微細藻類を培養増
殖する。得られる微細藻類を粉砕してそのまま燃料とす
るかまたは微粉炭・水スラリーや重油等の炭素質燃料に
添加して燃料化する。この燃料を火力発電の発電燃料と
して使用する。
A large amount of carbon dioxide-containing waste gas generated from a thermal power plant is supplied to a carbon dioxide separator to be separated into carbon dioxide and other gases. The separated carbon dioxide is directly or once stored as liquefied carbon dioxide and then supplied to the microalga culture tank.
Microalgae are cultured and propagated in this culture tank by carbon dioxide and light irradiation. The obtained microalgae is pulverized into a fuel as it is, or added to a carbonaceous fuel such as pulverized coal / water slurry or heavy oil to convert it into a fuel. This fuel is used as power generation fuel for thermal power generation.

〔実施例2〕 以下、本発明の微細藻類の生産方法の一実施例につい
て説明する。
Example 2 Hereinafter, one example of the method for producing microalgae of the present invention will be described.

石炭火力発電所の炭酸ガスを11%含有する温度約110
℃の廃ガスをアミンへの吸収またはゼオライトへの吸着
によってNOx、SOxその他のガスから炭酸ガスを分離す
る。このように炭酸ガスのみを含有した吸着剤を加熱そ
の他適当な手段を利用して炭酸ガスを放出させて、1〜
5%の炭酸ガスを含む空気または液化炭酸ガスを得る。
これらの空気または液化炭酸ガスを、プラスチック屋根
付プールや少し傾斜させて培養液が流れるように構成さ
れた循環水路方式などのクロレラやセネデスムスの培養
池へ曝気、滴下その他適当な方法によって添加し、同時
に日光及び電球の光などで24時間照射を行い微細藻類を
繁殖させる。このようにして生産した微細藻類を炭素質
燃料に添加して燃料化する。
A coal-fired power plant has a temperature of about 110 that contains 11% carbon dioxide.
The carbon dioxide gas is separated from NOx, SOx and other gases by absorbing waste gas of ° C. into amine or adsorbing to zeolite. As described above, the adsorbent containing only carbon dioxide gas is heated to release carbon dioxide gas using other appropriate means.
Air or liquefied carbon dioxide containing 5% carbon dioxide is obtained.
The air or liquefied carbon dioxide gas is added by aeration, dropping or other appropriate method to a culturing pond of Chlorella or Senedesmus such as a pool with a plastic roof or a circulating water channel system configured such that a culture solution flows with a slight inclination, At the same time, microalgae are propagated by irradiating with sunlight and light from a light bulb for 24 hours. The microalgae produced in this way are added to a carbonaceous fuel to convert it into a fuel.

〔実施例3〕 次に、本発明の炭素質燃料の調製の一実施例を図面に
ついて詳述する。
Embodiment 3 Next, an embodiment of the preparation of the carbonaceous fuel of the present invention will be described in detail with reference to the drawings.

第2図において、1はホッパーを示し、ここに上記で
生産した湿った微細藻類Aを投入し、ホッパー1から適
量を脱水機2へ送入し水分を30%程度に調整する。次
に、定量供給機(図示省略)を経て混練機3で界面活性
剤など防腐、分散用等の必要な添加剤を加え、さらにミ
ル4で十分混合した後、1次貯蔵タンク及び送出ポンプ
(共に図示省略)を経て貯蔵タンク5に貯蔵する。
In FIG. 2, reference numeral 1 denotes a hopper, into which the wet microalgae A produced above is put, and an appropriate amount is sent from the hopper 1 to the dehydrator 2 to adjust the water content to about 30%. Next, a necessary additive such as a preservative and a dispersing agent such as a surfactant is added in a kneading machine 3 through a constant-rate feeding machine (not shown), and the mixture is sufficiently mixed in a mill 4. (Both not shown) and stored in the storage tank 5.

11は既存の石炭水スラリー(CWM)や重油の貯蔵タン
クである。
11 is an existing storage tank for coal water slurry (CWM) and heavy oil.

また、Bは真空乾燥や天日乾燥によって乾燥された微
細藻類の粉体である。
B is a powder of microalgae dried by vacuum drying or solar drying.

本発明の炭素質燃料は、上記貯蔵タンク11内の炭素質
固体粉末、分散剤、安定化剤、水を主成分とする炭素質
固体・水スラリー組成物(A)または重油などの炭素質
液体組成物(B)に、 i)上記貯蔵タンク5内の水分約30%の湿潤微細藻類を
混合機6内で混合添加するか、燃焼バーナー12への燃料
供給管中へ第1図に示すように直接添加するか、 ii)上記Bに示す乾燥微細藻類を燃焼バーナー12の直前
で添加するか、または混焼バーナーを使用して、あるい
は iii)上記i)とii)の併用によって、 たとえば、石炭火力発電所のバーナーへ炭素質燃料とし
て供給される。
The carbonaceous fuel of the present invention may be a carbonaceous solid powder, a dispersant, a stabilizer, a carbonaceous solid / water slurry composition (A) containing water as a main component, or a carbonaceous liquid such as heavy oil in the storage tank 11. To the composition (B), i) a wet microalgae having a water content of about 30% in the storage tank 5 is mixed and added in a mixer 6 or into a fuel supply pipe to a combustion burner 12 as shown in FIG. Ii) by adding the dry microalgae shown in B above immediately before the combustion burner 12 or by using a co-firing burner, or iii) by using the above i) and ii) in combination. It is supplied as carbonaceous fuel to the burners of thermal power plants.

そして、燃焼ショウ発生する廃ガス中の炭酸ガスは前
記第2の発明について説明したように微細藻類の培養に
利用され、光合成による炭酸ガスからの微細藻類の生産
とその燃料化によるリサイクルが成立し、炭酸ガスの回
収とその再利用が有効に行うことができるのである。
Then, the carbon dioxide gas in the waste gas generated by the combustion show is used for culturing the microalgae as described in the second aspect of the invention, and the production of the microalgae from the carbon dioxide gas by photosynthesis and the recycling by conversion to fuel are established. Therefore, the recovery and reuse of carbon dioxide can be effectively performed.

〔発明の効果〕〔The invention's effect〕

以上のように本発明によれば、地球の温暖化その他環
境上いろいろ問題のあった廃ガス中の炭酸ガスの回収と
その再利用を効率的に行うことができ、炭酸ガスのリサ
イクル方法が確立できた。
As described above, according to the present invention, it is possible to efficiently recover and reuse carbon dioxide in waste gas, which has various environmental problems such as global warming, and establish a method for recycling carbon dioxide. did it.

そして、藻体1kgを生産するのに使用炭酸ガスの利用
率50%として約3.4kgの炭酸ガスを必要とするために多
量の炭酸ガスの回収が行われるばかりでなく、炭酸ガス
の温度が高いものを利用すれば冬期でもクロレラやセネ
デスムスの生育適温25℃を維持できることはもちろん、
35〜40℃を適温とする藻株を用いて単位面積当りの藻類
の生産量を挙げて、化石燃料の使用比率を低下させて省
資源を一層高めることもできる。
In addition, since about 3.4 kg of carbon dioxide is required to produce 1 kg of algae with a carbon dioxide utilization rate of 50%, not only a large amount of carbon dioxide is collected, but also the temperature of carbon dioxide is high. Of course, if you use it, you can maintain a suitable temperature of 25 ° C for growing Chlorella and Senedesmus even in winter,
The algal production per unit area can be increased by using an algal strain having an appropriate temperature of 35 to 40 ° C., and the use ratio of fossil fuel can be reduced to further increase resource saving.

さらに、炭酸ガスの吸収力が強く、かつその保持力が
強い藍藻スピルリナを使用して炭酸ガスの利用率を約80
〜90%に高めたい場合にも、NOx、SOx等が分離除去され
た炭酸ガス含有率11%の空気を利用することにより、ス
ピルリナ生育の最適pH9〜11に悪影響を与えることなく
炭酸ガスの回収を一段と効率良く行うこともできる。
In addition, using the cyanobacterium Spirulina, which has a strong carbon dioxide absorption capacity and a strong retention capacity, reduces the carbon dioxide gas utilization rate to about 80%.
Even when it is desired to increase to 90%, the use of air with a carbon dioxide content of 11%, from which NOx and SOx are separated and removed, allows the recovery of carbon dioxide without adversely affecting the optimal pH 9 to 11 for spirulina growth Can be performed more efficiently.

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

第1図は、本発明の炭酸ガスのリサイクルの概念図、第
2図は、本発明の微細藻類を含む炭素質燃料の調製の一
実施例を示す工程説明図である。
FIG. 1 is a conceptual diagram of carbon dioxide gas recycling of the present invention, and FIG. 2 is a process explanatory diagram showing one embodiment of the preparation of a carbonaceous fuel containing microalgae of the present invention.

Claims (5)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】炭酸ガス含有廃ガスを発生する火力発電所
等の工場に微細藻類池を併設し、当該廃ガスから炭酸ガ
ス分離器により、又はアミンへの吸収若しくはゼオライ
トへの吸着により炭酸ガスを分離し、当該分離した炭酸
ガスを、光合成を利用して微細藻類に固定し、得られる
微細藻類を粉砕して炭素質燃料に添加して燃料として再
度、火力発電所等の工場へリサイクルさせることを特徴
とする炭酸ガスのリサイクル方法。
(1) A microalgae pond is installed in a plant such as a thermal power plant that generates waste gas containing carbon dioxide, and the waste gas is separated from the waste gas by a carbon dioxide separator or by absorption into amine or adsorption to zeolite. , And the separated carbon dioxide gas is fixed to microalgae using photosynthesis, and the obtained microalgae is crushed and added to a carbonaceous fuel to be recycled as fuel again to a plant such as a thermal power plant. A method for recycling carbon dioxide, characterized by the following.
【請求項2】以下の(A)若しくは(B)の組成物又は
(C)の混合物に、請求項1記載のリサイクル方法によ
り生産した微細藻類が添加された、微細藻類含有炭素質
燃料。 (A)(a)石炭、オイルコークス、石油ピッチ系など
の炭素質固体粉末、 (b)少なくとも1種の分散剤、 (c)少なくとも1種の安定化剤及び (d)水 を主成分とする炭素質固体・水スラリー組成物 (B)重油などの炭素質液体組成物 (C)上記(A)の炭素質固体・水スラリー組成物と上
記(B)の炭素質液体組成物との混合物
2. A microalgae-containing carbonaceous fuel obtained by adding a microalgae produced by the recycling method according to claim 1 to the following composition (A) or (B) or a mixture of (C). (A) (a) carbonaceous solid powder such as coal, oil coke, petroleum pitch, (b) at least one dispersant, (c) at least one stabilizer, and (d) water as a main component. (B) Carbonaceous liquid composition such as heavy oil (C) A mixture of the above (A) carbonaceous solid / water slurry composition and the above (B) carbonaceous liquid composition
【請求項3】微細藻類が界面活性剤を添加されたスラリ
ー状物である請求項2記載の炭素質燃料。
3. The carbonaceous fuel according to claim 2, wherein the microalgae is a slurry to which a surfactant is added.
【請求項4】微細藻類が粉体である請求項2記載の炭素
質燃料。
4. The carbonaceous fuel according to claim 2, wherein the microalgae is a powder.
【請求項5】微細藻類が界面活性剤を添加されたスラリ
ー状物および粉体である請求項2記載の炭素質燃料。
5. The carbonaceous fuel according to claim 2, wherein the microalgae are a slurry and a powder to which a surfactant is added.
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